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Liquids - Science topic
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Questions related to Liquids
please i would like to collect all the parameters related to the synthesis of nanoparticles using laser ablation, in terms of laser parameters, liquid parameters, environment parameters and if any other parameters
Thanks
Which part of the Earth receives the least sun's rays and what part of the water cycle is when liquid water moves through the soil to become groundwater?
Which shape of water surface will give the highest rate of evaporation and why does water Vapour takes up more space than the same amount of liquid?
When the rate of evaporation equals the rate of condensation does the partial pressure of a volatile liquid in a sealed container change?
Why do liquids with fewer polar bonds evaporate faster and rate of evaporation of a liquid related to the intermolecular forces acting on it?
I extraction RNA from Physcomitrella patens (Moss) Following the protocol of RNAiso Plus. Firstly using a tissue lyser and added 1 ml RNAiso plus and vortex. next step Add the chloroform after centrifuge I separated the top liquid layer but the problem is yellow color liquid. I could not avoid the yellow color at ned of the extraction process after the precipitated pellet is brown.

Does the higher boiling liquid have stronger intermolecular forces than the lower boiling liquid and high viscosity mean strong intermolecular forces?
Why solubility of solid in liquid increases with increasing temperature and effect of temperature in the change from solid to liquid?
While in piezoelectric ceramics, a liquid phase can be observed easily with a conventional solid method preparation, however there seems to be no research to figure out whether the liquid phase can affect the mechanical quality factor (Qm) of ceramics.
How can we increase the solubility of a solid in a liquid and hHow does solubility of solid changes with temperature?
What increases the rate of dissolving a solid and factors that affect the rate of solubility of a solid into a liquid agitation temperature and surface area?
Hi,
Iβve recently started having issues with a Zeiss axio cam HRm camera. The cameraβs serial number and other informations are available below.
The problem is that something is obscuring the left part of the cameraβs field of vision (see attached picture taken by the camera). This issue is specific to the camera, not the microscope, because it is still present even when detached from the microscope. When I look inside the camera I do not see anything visibly blocking the sensor. The camera always stays connected to the microscope from the left side so no dust/liquid/condensation should have been able to gather on the sensor.
Does anyone have any idea what could be responsible for this issue, and how to solve it?
Camera information:
axio cam HRM
60 N-C 1" 1,0x
Serial number: 1 02 02 1247 Β Β r2.0
axiocam b/w Β Β Β Β Β Β Β Β Β Β Β Β Β Β 12v DC
000000-0445-553 Β Β Β Β Β Β Β Β Β Β 0.7A
ITE 93JA
Why do liquids have a fixed volume but not a fixed shape and what happens to the density and temperature of a gas as it expands?
I am working on Dead gene. my work is related to liquid liquid phase separation for cold shock response and i want to design primer for this amd i have not eniugh information how to select DNA sequence. and than choose c-terminao region to knockout mutants . i want some help in this regard.
One could argue that when R = KLaf ( Cs - C), the fugacity (the maximum transferable rate) has been reached and so the OTR or Rd is zero at that gas flow rate representing the energy input. However, this is a state that could not exist at that given gas flow rate, because OTR can never be zero in a respiring system. The case in which R = KLaf (Cs - C) is not a stable situation (i.e., not a steady state and C β CR), which implies that the actual transfer rate, as opposed to total potential oxygen transfer rate, to the liquid is less than R and the DO concentration is decreasing because the consumption rate has exceeded the transfer rate so that the system is now outgassing oxygen. However, this does not mean Rd is negative. That is, the actual transfer rate, the net oxygen transfer rate given by Eq. (10a), i.e., OTR = KLaf (Cs β C) β r, is not KLaf (Cs - C). To maintain a given DO set point, the air flow rate (AFR) would have to be increased to a new KLa value such that ultimately R equals the actual transfer rate to the liquid. A change in air flow rate would result in a different transfer efficiency, at least in a fine bubble system where an increase in air flow decreases efficiency, and so the true C* also would be nominally different (higher, actually, due to lower gas side depletion), but eventually a steady state would be reached in which the oxygen consumption (R) would exactly match the oxygen transfer rate. For any further increase in the organic loading rate (OLR) and if C > 0, the system can respond by lowering C so that the driving force increases, giving more impetus to transfer. However, when the consumption rate exceeds the oxygen transfer rate, CR approaches C, which itself is ever-decreasing, such that dC/dt is a decreasing function of the consumption rate, i.e., dC/dt < 0. Therefore, the system is no longer in a steady state in such an event. Eventually a point is reached at which C becomes vanishingly small such that even the maximum fugacity is not enough to satisfy, and so the only remedy is to increase the gas flow rate again to match the demand. The conclusion of this exercise is that, for submerged aeration in which the gas loss rate from the system is significant, the rate of transfer under the action of microbial respiration must be given by Eq. (12b) i.e., dC/dt = Kla (Cs β C) β 2Ru, in which both the associated liquid phase oxygen equilibrium concentration (Cs) and the apparent oxygen saturation CR will decrease accordingly (such a phenomenon can be experimentally verified in a converse manner by a reduction in the microbial GDP (the resistance due to biochemical reactions), the net result of a dilution is that both the associated liquid phase oxygen equilibrium concentration Cs and the apparent oxygen saturation CR will increase accordingly. (It is notable that the latter increases faster than the former, so that at R = 0, the rise of CR catches up with the rise of Cs, and so both become one and the same, C*inff).
Mines' paper began on the right track by citing Bartholomew, Albertson and DiGregorio, and some others like Eckenfelder, that there is definitely a relationship between KLa and OUR and so Mines conducted his experiment. Herein lies the difference: Those previous researchers used plant operation data, where the DO is maintained constant. One can only have either constant DO or constant AFR (aeration gas flow rate), but not both. Mines' attempt to verify the dependency of Kla on OUR is premised on constant AFR which is exactly right but he used the wrong equation, resulting in Table 3 and Table 4 that yield the strange result that at steady-state, the OUR is not the same as the OTR. Had he used the right equation, he would have got a consistent result that would support my theory. The consequence of an increase of Ru can only be a reduction of OTR for a constant AFR. It can never by an enhancement! Mines' equation 6, stating that Rd = KLa (Cs- C) - Ru + Ri is therefore insupportable.
His experiment needs to be repeated, but with the following caveat:
equations must be correct, i.e., equation 7 must be written OTR = alpha KLa(beta Cs - C) β Ru resulting in the accumulation term as:
dC/dt = Kla (Cs β C) β 2Ru
OUR of the mixed liquor suspended solids as determined by Method 213B in Standard Methods must be modified to eliminate the shaking effect;
the OTR should be independently measured by the offgas method to compare with the modified Equation 7, since the offgas method is widely considered the best way to determine OTR.
It is important to recognize that the transfer equation given by Equation 1 in Mines' paper, is only valid when R = 0. When R changes, both Cs and OTR will change, even though C changes, (decrease to increase the driving force, or increase if the AFR increases).
When the rate of evaporation equals the rate of condensation does the partial pressure of a volatile liquid in a sealed container change why or why not?
Does stirring increase the rate of solution of a solid in a liquid and how does sugar dissolve faster in water when it is stirred?
What happens to the viscosity of a liquid when temperature increases and why viscosity of gases increases but viscosity of liquid decreases with increase in temperature?
What is the rate of evaporation in dynamic equilibrium and constant temperature at which the vapor pressure of the liquid is equal to the atmospheric pressure?
Hi everyone,
I am currently working on batch experiment to quantify metal adsorption onto different materials. Because the variation of pH after addition of the material is significant and that we don't want to adjust the pH after addition (I am afraid it might impact the surfaces of the material), I wanted to know if a buffer solution can be used to limit the impact of the pH variation.
Also, I noticed there are two ways of doing batch sorption experiments: Lot of researchers varied the initial concentration keeping a fix Liquid to solid ratio to calculate the qe but others varied the liquid mass and the solid mass and maintained the Cini. What do you think are the best approach and what are the pros and cons of each?
Thanks in advance for you help!
Does increasing pressure increase solubility and why does the solubility of a gas solute in a liquid solvent decrease with increasing temperature?
Which condition will increase the evaporation of water and liquids have high viscosity and what do we call the ability water has to flow upward against the force of gravity?
Does surface tension depend on the type of liquid and what do stronger intermolecular attractions cause liquids to have?
specially about the gradual freezing do we need a gradual freezing for animal tissue like cell culture in liquid nitrogen ?
The Biuret protein method uses liquid samples. But how can I obtain a liquid protein extract from solid samples? Can you please share with me some methods or references about it?
Hi, I am Yuan and I am new to this experiment. I aim to express a protein by pGEX construct (Ampiciline), I used BL21 to do transformation, and I got some colonies on the plate(LB Amp) but when I grew them in the liquid medium. They didn't grow at all.
I am very sure I have picked up the colonies and they were in the medium. I tried a few times of transformation before I got this plate with colonies(Attached). I am very confused about it. Because If they could grow on the plate, why couldn't they grow in the medium which has the same recipe other than It has agar?
I would appreciate it very much if I could get any help. Thank you very much!

In the liquid phase sintering of Tungsten-Iron-Nickel powder compacts, could the presence of carbon (between 0.6% and 1.5%) significantly influence the final microstructure by altering the diffusion and the precipitation of W in the Fe-Ni matrix?
The available materials are autoclavable glass, kork, plastic
First, I mixed Hydroxypropyl Methylcellulose with DI-Water till homogeneous, then I poured KOH solution into the Hydroxypropyl Methylcellulose mixing and heated to 60 - 65 degrees Celcius.
The fatty acid was heated to 65 - 70 degrees Celcius to liquid and poured into the Hydroxypropyl Methylcellulose - KOH mixing (main tank), btw the temperature of the main tank after putting fatty acid increased to 8 - 15 degrees Celcius. Is the increase possible from the fatty acid solution or the reaction of fatty acid and KOH solution? How to control the temperature main tank around 70 - 75 degrees Celcius?
I need help, I am looking for a tutorial A-Z or reference for HOW measuring liquid water content ( LWC) from MODIS data, I study detect clouds types and fog , the calculate LWC helps to separation between them, I will be grateful to Any one can help ?
How do microbes help clean the environment and role of microbes in liquid waste management?
How can we convert a colloidal nanomaterial into powdered form.
I want to synthesize the peptides in liquid medium by using amino acids, but I don't have idea of synthesis of Pepetide in liquid medium. Please suggest if anyone has any idea about this.
To check the metabolites of blood , I want to use LC-MS/MS. So I want to know more about the sample preparation and is there any method to convert liquid sample into solid or semi solid form.
After centrifugation, I pass the suspension through the syringe filters, but the bacteria still grows in the culture medium.. How can I completely remove it from the culture? (Autoclaving and tyndallization should not be carried out).
I couldn't find the best system, can you help me?

I am a final year Masters's Student from Heriot-Watt University currently working on my dissertation project titled "A THEORETICAL ASSESSMENT OF THE STRUCTURE OF A LIQUID STORAGE TANK UNDER SEISMIC FORCES" with the following objectives:
1. Verification of Current Theories (Housner, Preethi, and Malhotra) of liquid Structure Behavior (sloshing wave height) under seismic forces for petroleum-filled storage tanks using Finite Element Modelling and Finite Element Analysis.
2. Assessment of the possible failure mechanism of the superstructure of the various liquid storage vessels under exposure to seismic forces using Finite Element Modelling and Finite Element Analysis based on the API 650 Design Standard.
3. Proposal and initial assessment of the effectiveness of a Bass Isolation System on the sloshing wave height using Finite Element Modelling and Finite Element Analysis.
Can the Ansys modal analysis module be used to model a fluid-filled storage tank and determine the sloshing wave height along with the impulsive and convective mass components of the fluid based on the application of specific Acceleration, Velocity, and displacement values?
Can I subsequently transfer the model to the Ansys Static Structural Module to determine the various resulting stresses that will develop within the tank structure due to the seismic forces and the fluid-structure interactions?
If not, can you guys offer any advice on what methodology I should take?
The package says 1 mg but the data sheet specifies "1-2Β mg/mL in Tris-buffered saline". Any recommendations? I need to prepare coated flasks with 20 ug/mL. Thanks in advance!
if i have two independent variables-mango peel liquid fertilizer group and commercial fertilizer group and dependent variables are: plants height, width and number of leaves.
There is a control group.
Hello,
I want to grow bacteria on glass coverslips by immersing them in a liquid bacterial culture. I would like to fix them to the bottom of petri plates or well plates , because otherwise they float in the medium. I've tried double sided adhesive tape, but when I try to remove the cover glass slip for fixation, they often shatter since they're strongly adhered to the tape. I would like to remove them from the original container because after fixing I need to adhere them to substrates with carbon tape for SEM visualization.
Are there any recommended techniques for fixing the cover slips in place during inoculation and then easy removal afterwards?
Thanks in advance.
Hello everyone,
I am struggling to find a better way to test the transparency of my hydrogels made of kappa carrageenan and/or with salts. I tried testing a 2cm thick hydrogel but the absorptance value reached above 1. I haven't tried using a cell with a liquid phase of the hydrogel.
I'd be glad to read your suggestions.
Thanks!
When hot and cold water are mixed the entropy increases and liquids have higher entropy?
Does entropy increase or decrease from gas to liquid and gas is dissolved in liquid entropy and does entropy increase from gas to gas?
hi anyone
Does the spectrophotometer measure solid particles or only liquid matter? Greetings
Why transfer of heat takes place faster in liquids than in solids and what is the process where heat flows in the absence of any medium?
Is it possible to create a 100-um thick polyimide layer through spin coating? If possible, What will the pi liquid's spin speed and viscosity?
Do mixing two liquids increase entropy and what happens when hot water and cold water mix?
Do mixing two liquids increase entropy and what happens when hot water and cold water mix?
What is a mixture of two liquids that are mixing together and when two liquids are mixed together and a new solid is formed?
What happens when two liquids of different temperatures are mixed and when two cups of cold water of the same temperature are mixed the water will be twice as cold?
What happens to entropy when a liquid change to a gas and what happens to entropy when liquid is converted to Vapour?
Is entropy increases when a liquid freezes at its melting point and what is the change of entropy on melting?
I want to know if the OTS comes in solid or liquid state and also how to make the OTS solution, which solvent to use for the desired purpose.
The phase transition from solid to liquid must be sharp and at 8 Celsius degrees. Other properties of the material are less important
Thanks
Yosi Scolnik
I've done research on that, but I haven't found any suitable sensors to use. Please help me
Can cement and liquid sulfur be used in a concrete mix at the same time?
Can asphalt and liquid sulfur be used in a concrete mix at the same time?
Hello,
What is the surface tension of Sodium chloride (NaCl) 0.9% (saline solution)?
At air/liquid interface
At 25 Β°C (and 20 Β°C)
Thank you in advance for your help π
It can act as an anti-inflammatory, energy-booster, antioxidant to strengthen your body's immunity and memory.
view: https://rasayanam.in/
The specific heat of oil that I have in my hand is known. I want to know what is the specific heat of it at higher pressure levels (not higher temperature)? Is there any instruments available to measure it directly or Is there any empirical relations to calculate it? The liquid I have is a hydraulic mineral oil.
- Formulation of OSD requires knowledge of some physicochemical constants of API, such as pka, logP, In order to better determine the BCS
But in liquid preparations, do you need to know that?
Hello,
What does mean when I get If= 0 in Freundlich adsorption isotherm for liquid where the R2 is 1.00 for the experimental data analysis in this model?
solubility in water: slightly soluble
solubility in acids: decomposes
How can I perform life time decay measurement of rare earth doped strontium sulfide in liquid form. As I have life time decay measurement facility which uses samples in liquid form only.
for example we have Gasoline tank and we want to know its empty or full
by ultrasonic
we have air gap
Hi all,
In the Young's equation, Οsg = Οsl + Οlg β
cosΞΈ.
When the surface tension of liquid( Οlg ) is known, surface energy of solid(Οsg) is known too.
After measure the contact angle between solid and liquid,
Is it possible that the interfacial tension between the liquid and the solid(Οsl) be negative?
If a negative value is valid, does that mean it is exothermic when forming a solid-liquid interface?
I have read a paper: https://www.nature.com/articles/nmat1336a
However, I still cannot determine whether negative surface energy is reasonable or not.
Thank you very much.
Sincerely
In the biofertilizer research there are two formulations 1) CARRIER BASED
2) LIQUID FORMULATIONS
Which one is more effective in the field?
I used a Domiphen Bromide in the concertation of 0.025 w/v as preservative in the oral liquid formulation.
Its effectiveness has been proven by the Antimicrobial Efficacy Test.
Is it used concentration in the range of recommended concentrations for this preservative.
suppose X is the total polarizability and x1 and x2 are individual polarizabilities. So will the final result be X=x1+x2?
Please help.
I have a cell line that is vulnerable to liquid N2 and vapor phase nitrogen storage. I am looking for any homemade protocols that allow long term storage of cells under -80oC to -100oC preferably in a ultra low temperature freezer.
I am working on pressurized liquid heat transfer related problems. I got correct flow regimes for heat transfer at atmospheric pressure. Now I need to pressurize the fluid more than 300Bar and analyse how the heat transfer occurs. Even though we approximate liquids to be in-compressible, beyond 300bar the volume reduces hence the change in density comes into picture. how to model this in Ansys? What should be given in density column in material properties of liquid? I tried with compressible-liquid option and I am not getting correct flow regimes. I should find how the transfer occurs at elevated pressure ranges. Need your help!!!
Thanks
I have a mixture of goat serum / plasma that I attempted to ammonium sulfate precipitate (using pooled samples) to get out the immunoglobulins. I dialyzed in PBS afterwards, but when placed in the fridge, it became a jelly-like substance. As this will need to be stored in the fridge for further uses, how can I stop the mixture from turning jelly-like? Also, how do I fix / revert the jelly-like solution back to liquid?
I'm doing PCR and qPCR frequently. My assay is extremely sensitive so I need to pipette a very exact volume from my SOP. From my experience and also my school lab course, I learned to press the pipette to the 1st stop to get the desired volume, and then press all the way to the second stop to expel all the liquid. However, I was harshly judged by my supervisor for using such skill. My supervisor said it must be done only at 1st stop, picking the liquid at 1st stop and expelling the liquid at 1st stop. I tried the above way but always left some residue on the wall of the tip, which raised my concern a lot.
My supervisor made a judgment that if I can't expel liquid at the 1st stop, it is my tech skill problem. I also asked some co-workers ( sophisticated), and some of them indeed stop at the 1st stop to dispense an accurate amount, and ignore the residue on the tip. One coworker advised because of the air pressure, angle, and speed when you pick the liquid, it might over-pick the liquid so dispensing at 1st stop is accurate enough.
My liquid usually thawed cold serum, enzyme, probes, and buffer, so I'm less concerned about evaporation. I'm grateful for any suggestions here!

Hello everyone, i need to calculate the activity coefficient πΎπ in order to calculate the mole fraction of a component in vapour phase from a given mole fraction of the component in its liquid phase using Raoult's law. I have found that for multi-component droplets, many literature has suggested to compute the value of πΎπ using UNIFAC method. UNIFAC method itself is computationally heavy and may not be possible to implement the entire method in the actual model for multi-component droplet evaporation. Is there any other analytical equation for calculating the activity coefficient which will be possible to implement in the model for multi-component droplet evaporation?
Have a nice weekend!
Regards,
Kapil Jaiswal