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Celebration of dried seafoods products.
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To make Japanese-style dried fish, the fish is cut into two pieces along the bone, the internal organs and gills removed, washed, and then soaked in a 3-5% by weight salt solution for about 30 minutes to 2 hours.
There are two things to keep in mind when drying fish in the sun.
1. Weather: The water activity of Japanese-style dried fish is about 0.86-0.88, so a sunny day with wind and a relative humidity of 0.70 or less is ideal.
2: Histamine risk: Histamine risk rises sharply when the temperature exceeds 30°C, so it is best to do it in months with as low a temperature and relative humidity as possible.
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vhjk dfdfgf
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How much you charge for publication book chapter on a particle, If it free of charge count me in for your book
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I've a nanomaterial dispersion in water. I want to recover the material in solid form. I have used freeze drying method earlier. Now I want to utilise another method? What would be a facile method for drying the sample properly and recovering the nanomaterial powder?
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Supercritical drying if you can disperse your material in Ethanol.
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We are having a seed dryer soon in our Farm. In our assessible markets, grain dryers are common but getting choices for seed dryer is not. I am concerned about germination of seeds if dried in grain dryer which doesn't have temperature control options. Please suggest me mechanical seed drying options suitable for a farm that produces seeds in about 30Ha of land.
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La temperatura que se sugiere es 15 grados celcius
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What are the precautionary measure that we can adopt to prevent the sprouting while drying the plant sample for herbarium?
Please suggest
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Microwave (or an oven) will act fine, killing the tissue. But change paper frequently after applying it, especially with succulents.
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What is the relationship between the variables affecting the design of the evaporator chamber with the diameter and height of the chamber?
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Yes, it can be determined.
The type of sprayer must first be specified to determine the distribution diameter range. Then, considering the cone angle of 60 degrees and also considering the co-current for the inlet flow to the chamber and the direction of spraying, the ratio between height to diameter in the evaporation chamber is considered between 0.6 to 1. However, it should be noted that to determine the maximum radius of the evaporation chamber when using a wheel atomizer, there is a relationship between the inlet volume flow to the wheel atomizer and the diameter of the disk.
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Dear friends,
Would you please provide me with the pdf format of the book Titled “ Spray drying handbook ” written by K. Masters. I look forward to receiving the file as soon as possible for my research project.
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Thanks.
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We have modeled hot air air drying of peppermint leaves and need some information about heat and mass transfer coefficients of the leaves to apply in  the model. Please help and guide me me,
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Any scientific study or technical report on anaerobic digestate thermal drying for pathogen destruction ?
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Yes possible but depends on the drying technique.... Thermal drying is the answer
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I need to work on a dry weight of shark liver and I couldnt achieve it through freeze drying
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Hadil Ossama Elsayed : Hi, curious to see what worked for you finally. I am having a similar issue, I want to dry shark liver samples for mercury analysis. I have already freeze dried and secondary dried (48 hrs) them. But some of the samples have a thick oily layer on them. Any advise appreciated. Thanks.
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Other than chilling method for preservation of Bombay duck (Harpadon nehereus) during rainy days?
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Dear Dr. KA Martin Xavier,
My point of view is simply this.
Those fish varieties which fetch more price by direct selling should not diverted in to the processing of protein concentrate.
There are several other varieties which can be processed to recover protein out of them.
Regards,
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What are the Governing equations (Heat and mass transfer Eq.) for a gas-to-liquid while injection from beside hot air and spray liquid downward jet in the cyclone-tape evaporation chamber?
When swirl gas in a cyclone on the small droplet liquid has impacted increased the resistant time and completed the evaporation processes.
For example, follow this Fig but the schematic upward spray jet with a circular nozzle.
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Luis Velazquez-Araque thanks so much for sharing
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The Corona Virus Epidemic poses an important challenge to practical hygiene on a mass level. Recent research has shown that in places where a great number of persons convene, toilets and wash rooms might be critical for reducing or enhancing spread.The effectiveness of various types of eletcric hand dryers hasbeen at the origin of heated discussions, but to show evidence the the presence or absence of microbes on the hands is just one factor. Other factots, such as the risk of contamination of surfaces surrounding the hand drying device or of the release of contaminated aerosol into the atmosphere surrounding the device. Who knows of more recent studies which have taken into account these elements?
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not 60%. FDA and WHO specify 75% ethanol or 80% IPA.
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In most sources i found Loss on drying /LOD (w/w %)of a sample is determined by putting about 1g of a powdered sample into an oven at about 105°C for some hours.
Afterwards it is placed in a desiccator while cooling.
This is not only used in most papers i found - but also mentioned in Pharmacopoeias or Certificates of Analysis.
In a few articles i found vacuum desiccators mentioned. But so far nothing about how those two methods compare. Or if it is even possible to get comparabe/accurate results when using a vacuum desiccator with siliga gel instead of an oven?
Does anyone of you have experience in drying powdered samples (e.g. herbal extracts) and determing LOD via vaccum desiccator?
How do the two methods compare? How long does it need roughly to dry?
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We generally use vacuum drying when a sample are heat-sensitive, or when high temperature cause gelling in the sample. 50C at overnight is the generally accepted method. Keep in mine that water can be produced by thermal reactions, misleading your results. If your sample is not heat-sensitive, then you should be no worry since you use one of the standart methods. I used 3 methods to comapre LOD in a food sample. I found that thermogravimetri was the best one among them (oven and vacuum oven)
Good luck
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I work with ceramic aqueous suspensions which I pour into a 3D-printed mold. My current problem is the fact that water evaporates too quickly from my samples, causing bubbles and other dislocations that affect structural integrity. I am currently trying to iron out a process which utilizes an H2SO4/H2O mixture that can create a constant humidity environment inside of an empty desiccator, but many times it has been unsuccessful. Any other ideas or reccomendations would be appreciated as to how I can mitigate this issue.
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Hi Alex,
your bubbles are probably not caused by evporation of water but by entrapped air from the previous mixing procedures. De-air your suspensions before casting (200 mbar vacuum while stirring, if necessary add a de-foaming agent).
We often do slip casting of square sample plates in silicon frames placed on plaster plates. In order prevent evaporation and drying out of the samples on the top we cover the molds with thick and stiff plastic foil with some weight on top.
Frank
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Hi all,
I'm trying to make some conventional Li-S electrolyte which requires the addition of LiNO3. This chemical is relatively hydroscopic and even the anhydrous one contains quite a lot water. One thing about LiNO3 is it's a strong oxidizer that has the potential of explosion, so I'm hesitant about using common salt drying method (vacuum oven at high temperature). There's also much in literature indicating how did they make their electrolytes and dry LiNO3. Would anyone who's also doing Li-S study tell me how do you dry your LiNO3 salt?
P.S. This is just a thought about justifying using common vacuum oven method to dry oxidizers like LiNO3. Under vacuum, even know LiNO3 is a stronger oxidizer, but there isn't fuel in the oven that can cause fire. After vacuum heat, I can let the temperature drop to room T first before refill the chamber with air, or refill it with Ar. Does it make sense?
Thank you!
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The commercial LiNO3 salt labeled 'anhydrous' can, in principle, be dried by 120—180 ºC. Not so dry salt can be dryed at 180 ºC for a few days, and/or by fusing under vacuum, preferably more than once.
You may refer to the signalled paper:
F.G. Donnan, B.C. Burt, "XXXV.—The solubilities and transition-points of lithium nitrate and its hydrates", Vol. 83, 1903, 335-342.
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I am looking for an efficient way to dry rice seed after surface disinfection and inoculation with fungal spores. Literatures mentioned that they did air dry, but this did not seem to be insufficient to me. it might take hours to dry 3 ml of suspension that i am going to use. The limitations are the samples should not be exposed to high temperature which might inactivate fungal spores and blowers that would cause spreading of fungal spores after drying. Does anyone have a good idea?
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Expose the seeds to cold plasma.
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I'm working on a project which requires me to bring down the Relative Humidity of my test chamber (150mmx150mmx150mm) to <10%. I would like to know if this is achievable through the use of desiccants such as molecular sieves and silica gel?
(assuming experimental conditions of 20C ambient and chamber temperature and initial RH of 80%~90%. from the total volume of air and relative humidity, my calculations tell me that I need to remove 0.06g of water since my chamber is relatively small in size. But this number seems abit sketchy to me.)
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Hi Jonathan,
Your calculations are correct (assuming there is no sample that releases water). Well dried Silica gel (bentonite, Drierite etc.) will provide RH of >5%, of course you need to have excess desiccant. Without forced air circulation it will take longer time to reach the low RH due to slow diffusion but this can be optimized by a technical solution...
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Dear all, we need a procedure to rapid drying plant materials from field or greenhouse experiments to rapidly denaturing enzymes, kills micro-organism and stabilizes the tissues. On one hand we want harvest hundreds of plants and cut it immediately into several parts (leaves, stems, ears and so on) in a short time to avoid changes in daily sequence of metabolic processes. Drying over days in compartment dryer at 105°C or airing cabinet at 60-75 °C for 24 or more hours is not possible because we would need too much for 100 or more plant sample daily. On the other we want determine the dry matter and analyze the content of nitrogen, carbohydrates and other compounds in it after drying without losses. Which power rating (watts) can you recommend, which sample size, when a constant weight will be achieved: 5 minutes, 10 minutes or how many? Have published your experiences with simple domestic microwave ovens anywhere? Commercially microwave ovens are to expansive for us in the moment. Thanks for your answers, regards Petra
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Microwaves are initially not drying a sample, but heating the water within the sample. This is cooking your sample while it gets finally dry or even burnt. If the samples are tea leaves, then the tea may taste quite differently than usual.
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I am working on Aloe vera gel processing and product preparation. Aloe gel drying is carried out in freeze drying resulted good quality. In which method ,the biological active component  are minimum affected so we can made use of Aloe gel in cosmetic products.
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Above Article should be helpful
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I'm trying to obtain equal absorption rates of silica gel along a temperature gradient (20 - 40 °C) by adjusting the weight of the silica granules. Is there any literature on the relationship between temperature and absorption capacity (or a formula) of silica gel that can help me calculate this? The silica that will be used are 'shop-grade' pellets.
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To determine the adsorption capacity for your silica gel you first need an equation of adsorption equilibrium to combine it with the equation of adsorption rate. As an equation of adsorption equilibrium you can use the Langmuir or Freundlich models that are well known, or another that fits your experimental data. Once you determine the adsorption equilibrium model you can use the Arrhenius' equation to represent the dependence of the parameter related to the maximum adsorption capacity with respect to the temperature in the model.
As the amount of water adsorbed is a function of both the moisture concentration in the gas surrounding the silica granules and the temperature, it is necessary to perform test at various relative humidities with constant temperature and at various temperatures, to find the parameters of adsorption rate and also the parameters of adsorption equilibrium.
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I need a Comprehensive Review paper on the Application of Artificial Neural Networks (ANNs) and Genetic Algorithm (GA) in Drying Technology?
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In case you need more, try this;
Application of Artificial Neural Networks (ANNs) in Drying Technology—A
Comprehensive Review
Mortaza Aghbashlo, Soleiman Hosseinpour, Arun S. Mujumdar
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Hello dear researchers,
I am doing some experiments with the freeze-dryer at the moment and I am experiencing a temperature anomaly that I cannot explain.
I tried it with pure water, 1M sucrose in water and water+protein, same result for every sample.
The following happens:
I freeze the samples in glass vials at -70°C shelf temperature for 8 hours, and enable the vacuum at the 8:30h mark. As soon as the vacuum pump starts working, the temperatures of the samples start dropping. That is clear to me, because the sublimation removes heat from the samples.The thing that is not clear to me, is why the temperatures start rising pretty soon as the vacuum gets stronger, and even rise above the value they had before the vacuum was enabled.
There should also be a picture attached. The lines that make the curves are my sample temperatures, the pink line is the pressure and the red line is the shelf temperature. (the picture is zoomed in, the pink line actually starts dropping right where the temperatures start dropping!)
Im happy about any suggestion I can get! Thanks!
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Hello Harald Schuchmann, thank you for your answer. -70°C is definitely the shelf temperature, at least according to the sensor. The problem is that the samples are always 15-20K warmer than the shelf after turning on the vacuum and since I am also working with sucrose solutions, their temperature should not exceed -40°C, because I dont want to get near the collapse temperature. Although the shelf is at -70°C, the sublimation still progresses. I see it because a dry layer forms on top, and the samples with pure water disappear.
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- Why are inorganic salts like LiCl, alcohols like TEG, some ionic liquids, or other materials such as cellulose hygroscopic?
- Are there different mechanisms for hygroscopic substances (liquid or solid) to absorb/adsorb/desorb water?
- Can somebody recommend any book or publication about the theory behind hygroscopicity?
Thank you.
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I doubt that it is possible to find one single book, which covers all this phenomenon. Hydroscopicity has a simple thermodynamic explanation but encompass too broad range of specific cases. It is a process of water transfer from its pure liquid through vapor phase to
(1) surface of hydrophilic adsorbent (eg. celulose), or the crystalline phase of hydrate (eg. that of cyclodextrin or inorganic salts), or the product of chemical hydration, like with CaO.
(2) liquid solution formed as a result of dissolution of a target solid substance in water vapor (eg. CaCl2, sugar, etc., )
(3) solution in liquid substance (eg. TEG).
Respectively, in the case of hydroscopicity, Gibbs energy of this transfer should be large negative. For this,
(1) Adsorbent should have metal cations, or hydroxylic, or peptide groups on its surface, or any combination of these. In other words, there should be both proton-acceptor and proton-donor centers in its pores. A crystalline receptor should be able to include or coordinate water;
(2) Solubility of a solid in water should be high; the data can be found in any handbook with properties of organic and inorganic substances;
(3) The liquid should have a negative or small positive parameter of hydrophobicity LogP, where P is a 1-octanol/water partition coefficient, which can be found in various databases or calculated by software available online.
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I have a solution of protein hydrolysate and I want to dry the solution without changing the peptide activity. Freeze drying unit isn't working and I need another method of drying the sample. Can I use a spray drier? What will be the protocol.
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I met on the expanses of the Russian Internet a low-temperature spray dryer, the inlet temperature is 30-50 degrees Celsius 
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Dear colleagues,
We are having trouble drying nanocrystalline cellulose as oven drying is not recommended as it results in major aggregation of fibers. Does anybody know any alternative to spray- or freeze-drying?
Thank you
Lucca Malucelli
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The morphological properties of the dried nanocelluloses are dependent on the particular drying method. Different technologies have been developed for drying nanocellulose at lab, pilot and large scale production. Drying is removal of a liquid from solid/semisolid/suspension nanocelluloses to produce solid product by thermal energy input causing phase change. Depend on the size of your material as well as what you are looking for (morphology, re-dispersion); you may select a right method for it. If any further inquiries, please feel free to communicate.
Hope this will help
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if we take out all amount of air from a plastic bottle means making vacuum in plastic bottle and after this close the cap on it, then bottle get small in volume into the earth environment, generally we say that volume of bottle has been decreased due to the difference of the air pressure, but if we take this bottle into the space where is no air then what happen 1) will the size of the bottle increase to get perfect bottle condition? or 2) it will remain same in size/volume?
if we open the cap of bottle then what happen? 1) will the size of the bottle increase to get stable condition? or 2)will  it remain same in size?
please give me the best suggestion because my research is in trouble condition without this solution.
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The increase in size of the bottle (i.e. return to normal) depends if there is a force that pushes the bottle walls from inside to restore it.
If you take all the air here in earth, then the bottle shrinks. If you take it to space, the bottle cannot restore its original shape, since there is no force (pressure) pushing from inside the bottle to restore it back to its original shape. Then 2) should be the correct (ideal) answer. This is the case of an inelastic material (like an aluminum bottle). Also, nothing should happen if you open the cap, since inside and outside the bottle remains in vacuum.
However, an exception would occur if the bottle is plastic, the force of the plastics themselves try to restore it to its original shape. This is due to elasticity of the material. If the material is elastic enough, it may return to its shape (like a rubber bottle).
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Harvest Right offers moderately large freeze dryers for food at a fraction of the cost of one from labconco, anyone see a reason why this would be a bad idea?
thanks
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Dear Miss Janice,,
This is a very remarkable and contemporary themes and good, the discussion on this developed!
What I want you to notice that my answer was not on this subject over to someone who specializes in organ transplants as well as I and probably the mistake came to this side!
Regards
Jasenko
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Hello im working on making a films of hydroxyapatite coated on polymeric phase but when I dryied it at ambiant air  i have seen some micro cracks on the surface. the cracks are not desired because after the calcination the mechanical strenght wil be very low. Can someone explain that phenomena even at low temperature
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Dear Khallok,
most of the  polymers  pick up water, when they are in touch with them. So while drying your  hydroxyapatite film your substrate is also is drying and a loss of water content close to its surface will take place. Thus the surface of your substrate shrinks giving rise to cracks in your film; even at low temperature.
Sorry, but polymers combined with water are always ugly issues from the experimental point of view.
You may use a very thin  polymer film rigidly attached to a stiff substrate. This main substrate cannot avoid shrinking of your polymer film but may reduce the degree of skinkage while drying.
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In most of the research papers deep-bed models are considered for studying the drying rate of agricultural crops in a solar cabinet drier.In these cases the deep-bed drier is considered a series of thin-layer model for analysis.So is it advisable to consider an experimental setup thin-layer.Is there any problem in doing so?
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the dept of the dryer is not the issue what matters is thickness  formed by the bed of the material being dried although your question is not really specific
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parboiling involves soaking,steaming and drying, how does these stages contribute to paddy breakage
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My publication entitled "Quantifying the relationship between rice starch gelatinization and moisture-electrical conductivity of paddy during soaking"
"Mathematical modeling of starch gelatinization and some quality properties of parboiled rice based on parboiling indicators using RSM"
 
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I wan to integrate NaSO4 pellets and NaCl as desiccant to aid continuous drying of tomato in a humid environment with limited sun.
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As you know each salt has a definite RH for example NaCl provides ERH of about 70 and it depends upon your aim at which RH would you like to keep your product or trying to equlibrate.
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pseudobulbs of Philippine Ground Orchid (Spathoglottis plicata Blume)
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Lyophilization
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I would like to understand the formula or ways to calculate the drying time and other variable parameters required to dry a food product using hot air. Known data are - initial product moisture, weight and expected final moisture, drying air temperature, air velocity. Drying time needs to be calculated. Can some one help ?
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Hi!
There are many aspects involving drying. Drying time will depend on the material, equipment being used and also the process' parameters. Spray drying will bring a quite different time from fluid bed, for instance. According to the drying process you'll have a different drying profile, then different drying times. Other point, some materials are better dried in specific drying methods, something that also impacts on the drying time.
Depending on the drying method you can estimate the drying time, using specific equations for that. Normally you can see a mix of theory and practice. You estimate the time and check/follow in the field. If it is a commercial dryer, talk to the supplier, it will have almost all needed information. With all paramaters presented by you, the drying time will be a function of inlet flow rate, that will vary from one drying process to other.
If you can, it is possible to use NIR for following the drying in line and determine when the drying achieved the desired point. If not, you have to take samples and identify the right time. If you are not achieving the right moisture, look at the process parameters. A DCCR could be used in order to optimize your process.
You have some references bellow and attached.
Hoping it helped.
Regards.
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Equilibrium moisture content
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EMC is mc of the material with the drying air or atmosphere in which it is being done. Know the mc of atmospheric air i.e. humidity  and and rate of mc removal at certain point indicates equilibrium mc.
 From drying experiment data, at a particular temperature,  you may determine the EMC value. Plot "Moisture removal rate (dm/dt)" with "Average moisture content (kg/kg)". Now extrapolate the plot and find the point where "Moisture removal rate"=0 and subsequently get the value of "Average moisture content."
The average moisture content value is the moisture content, where the moisture removal rate is "0", i.e. the point where the product reached EMC.
Dear experts, I need information about equilibrium moisture content for peppermint leaves to model dynamic drying curves. Could some one help me? - ResearchGate. Available from: https://www.researchgate.net/post/Dear_experts_I_need_information_about_equilibrium_moisture_content_for_peppermint_leaves_to_model_dynamic_drying_curves_Could_some_one_help_me [accessed Aug 23, 2016].
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I need some researches on the parameters affecting solar drying of date palm like air relative humidity and initial moisture content of dates 
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You can refer to these three articles - They are easily available.
1. Valorization Study of Treated Deglet-Nour Dates By Solar Drying Using Three Different Solar Driers
Samira Chouicha#a, Abdelghani Boubekri#a, Djamel Mennouche#a,Hamza Bouguetaia#a, Mohamed Hafed Berrbeuh#a
Samiha Bouhafs#a , Wahiba Rezzoug#a
doi: 10.1016/j.egypro.2014.06.109
2. SOLAR DRYING KINETICS OF DATE PALM FRUITS ASSUMING A STEP-WISE AIR TEMPERATURE CHANGE ABDELGHANI BOUBEKRI1,*, HOCINE BENMOUSSA2
DJAMAL MENNOUCHE1
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During drying, heat and mass transfer is commonly observed along with a change in volume (i.e. Shrinkage). Which tool should be chosen to model this process?
Thank you in advance.
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You may consider Stefan Problem approach to model shrinkage or swelling in a phenomenological mass or heat transfer model. In such approach one considers that one or two boundaries of the diffusion domain is free to move. This is physically observable and mass or heat balance equations may be written in order to describe the boundary movement. Here is an article where me and my colleagues applied and validated such approach to model hydration of soybean grains
Moving boundary modeling of conventional and transgenic soybean hydration: Moisture profile and moving front experimental validation 
doi:10.1016/j.ijheatmasstransfer.2015.07.014
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Im asking about the effect of the drying process from 35 C to 105 C on the final mechanical proproties of a prepared Alumina foam using a suspension coated on polymeic sponge 
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Dear Khallok, the drying process play important role in determining the mechanical properties since the green piece shrink to fill the volume occupied by water.  At the end of drying process internal structure of the piece will depend on the rate at which the water leaves the working piece and the structure shrinking rate.
Now the maximum integrity of this structure can be obtained when the shrinkage movement rate  is more or less about the rate of water removal.  In this case, minimum porosity and higher relative density will observe parallel with building a higher grain contacting area.  These conditions, for example, produce a function of increasing the compressive strength in terms of increasing the relative density.
This process optimization is highly affected by the drying temperature you designed between normal water temperature 25C and the boiling point temperature since this will affected both of the rate of water removal and the shrinkage movement rate. Therefore drying temperature affected the final mechanical properties mainly the compressive strength. 
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I am using a anionic drug (490mg) plus an adjuvant (250mg of Polaxamer 188) in 100mL of ultrapure water (Solution A)
Then using a mother solution of an anionic polyssacharide (10mg) in 100mL (solution B)
I pick 25mL of A and 25mL of B (50mL final) and spray dry
But, when I spray dry (Buchi Nano Spray Dryer B-90), I cannot recover anything because all of these solids stay in the particle collector wall.
I am wondering that:
1) the solution (A+B) is too moist, because i am using 60 celsius.
2) the solution have high concentration of drug/adjuvant.
3) Polaxamer 188 is non-anionic and I using two anionic compounds). But all cationic adjuvants that i searched (I.e. benzalkonium hydrochloride) show high pulmonary toxicity.
I have two options that i can try:
1) Change the temperature (60 to 100 celsius to observe that the moist is the problem)
2) Change concentrations of Polaxamer 188.
Anyone can help?
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Hi Max
Did you use exactly 100C? because that is still low.
I assume by collector wall you are referring to the cyclone?
Did you check the total concentration of solids you have in liquid. That's another reason why the particles may not reach the product collection tube if the particles do not have enough solids and are low in density. If you have a picture of the spray dryer and the deposit and you can send it to me, I can probably help you further. my email is ali_al-khattawi@outlook.com
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Dear friends,
I've prepared alginate nanocapsules which are in distilled water. How can I dry them other than freeze-drying and spray-drying methods? In other word, in order to get a dried and powdered capsules what method you suggest?
My goal is to evaluate their stability in the simulated gastric fluid (SGF), So I need dried form of them. For example, according to a paper, 20-30 mg of microcapsules added to a glass tube containing SGF. 
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Dear Sepehr,
how about vacuum drying. Thsi is available on small scales, too and more often found at university departments than freeze drying and spray drying.
good luck,
Harald
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I want to test a methanolic extract on cell line..however, my extract is not dry enough..the extract is still wet after being concentrated by rotovap..some people suggest just put it in oven at 60 degrees C but I am afraid the extract will be spoilt..please help
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Methanol and other organic solvents extract oils and resins from organic materials. When you concentrate the extract you end up with anything from and an oily liquid to a sticky resin or wax. It is not residual water that is making it oily or sticky, so you cannot dry it any further because it has almost no water in it. The oily/resin/waxy substance is the extract you are looking for.
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As soon is sample is inserted in the chamber at -80 C, bubbles starts forming and restricts the drying process. What could be done to avoid this.
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This is just my personal speculations on the matter:
1. Should your sample is liquid, bubble may have arisen from the entrapped tiny air or gas bubbles during the mixing  and merged back as an impact of molecular constrictions due to the thermal shocked of freezing.
2. May try to overcome it by: 1). do more careful or more gentle mixing during sample preparation and, use laminar flow mixing, if possible, to prevent from turbulence and eddy diffusion during the sample mixing; 2) degassed you samples by exposing it to vacuum pressure before you inserted into freeze dryer chamber.
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Hello,
we performed an easy drying experiment with a membrane wetted with water  by using a moisture analyzer. I have the data of weight change in time, temperature, moisture and membrane size. so is it possible for me to calculate mass transfer coefficent and diffusion coefficent from these data if so how can i do that ? 
Thank you.
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I think that you can get some useful information from the paper entitled "Assessment on thermal behavior of municipal sewage sludge thin-layer during hot air forced convective drying".
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We have a bench-top freeze dryer from labconco. But unfortunately our vacuum system with this dryer stopped working. Please suggest me an inexpensive vacuum system that we can add with the dryer. (please see the attached photo of the dryer). Thanks in advance.
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Mohmamad.
A scroll pump would be the ideal choice - more expensive than a rotary pump, but one then doesn't need to be concerned with regular oil changes.
All the major players (Pfeiffer et al.) make them.
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Calcination of feed happens while steam @ 400 Deg Celsius enter the dryer.
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Dear Santosh,
Please see the comparison  attached image,
Regards,
Prem Baboo
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We dry the sawdust before grinding in oven at 60 degree for 2 days but after grinding and seiving into different sizes the sawdust need to be dry again to begin reactions based on dry weight.
please help me as I am new master student in this feild
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I would suggest keeping the sieved sawdust in a sealed container with a constant relative humidity (using a salt solution).
Then you do the water content measurement in triplicate at the start of your experiments until you know it is maintaining the same water content. You can then account for the known water content in any future weighings/calculations.
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I want to get the aerogel of bacterial cellulose by freeze drying. But when i freeze bacterial cellulose in refrigerator, some ice forms outside the material, which differs from the ones frozen by liquid nitrogen. Could anyone tell me the reason of this difference and corresponding consequence?
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When you freeze samples slowly the temperatur at the outside is dropping faster than inside of your sample. Therefore the vapour pressure, which is a function of the temperatur is higher inside than outside => slow of vapour to the pressure sink, where it freezes as ice.
You have the same effect when cooling faster, but for a much shorter time.
Secondly your crystal size is smaller when freezing fast since the local supersaturation is higher => nucleation. For slower freezing the vapour grows alredy existing crystals.
Hope that helps,
Harald
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Could you give me a method in order to producing of a ""white"" dried mushroom powder "without" sodium bisulfite or other chemical materials?
mushrooms have very unstable colour, so during the drying process (eventually due to oxygen /hot air in tray drier) their colour immediately change to black. 
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In my opinion to prevent browning or darkening of mushroom slices you may soak them in 0.5% ascorbic acid( promptly after cutting )for a few minutes, then steam blanching the slices at 85-95 degrees Centigrade for one minute and finally vacuum or freeze drying to 5% final moisture content before grinding to powder.
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In my previous research, I used skim 10%, sucrose 10% and combination of both skim and sucrose (10%:10%) as cryoprotectant for freeze drying of Lactobacillus plantarum. I found out that the survival after freeze drying in presence of single skim and sucrose were higher than in the presence of combination of both. Is there anyone can explain how it could happened ?
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For freeze preservation of Lactobacillus can also be used TS  (Triptic Soy Broth) with  15% sterile glycerol, are maintained for several years viable
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I have purified a compound via HPLC, using water and methanol. the compound heat and light sensitive so my sample cannot be dried down via rotovap or other standard methods. i was planning on  freeze drying, but the methanol concentration is to high--around 80%--to effectively freeze so this is not an option either. i was thinking i could possibly use a high vac to evaporate the methanol and then use freeze drying. does this sound like a viable option? does anyone have any other ideas to separate my compound from solution. perhaps an ion column? its a polar carotenoid
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We generally extract aqueous methanol solution of carotenoids with diethyl ether. By the addition of more water the compound goes into the ether phase, which can be evaporated with roravap. We work with really sensitive carotenoids, but all of them can be evaporated with rotavap in a 40 C water bath.
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Design and fabrication of a dryer for maize on corn cobs.
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What is the material being analyzed?
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I have extracted surface layer protein from lactobacillus with 5M LiCl, dialysis against distilled water for overnight (approximately 20 hours) (5-10C), and freeze dry them. However, I found that some of the freeze dried powder will turn into liquid again (yellowish brown colour) and they cannot freeze into solid at -18C, thus I cannot freeze dry them again. Are they remains of MRS broth and how do I freeze dry all my proteins? I have tried to store the freeze dried proteins at -20C and room temperature (25C) and this problem still exist. 
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The presence of their lipid anchors and/or the Tween 80 might be expected to make your samples behave this way. Did you do the multiday dialysis against water these preps usually require? Tween 80 has a cmc in water of 12uM and is thus very hard to remove by dialysis.
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Is it necessary to dry the plant material to prepare an extract or extract/isolate/separate active substances (class of compounds or pure phytochemicals) from plant sources?
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It depends on the end product which you are going to extract and also on the availability of the plant source. If it is to be used for the whole year and it is harvested once a year; it has to be dried otherwise it will get spoiled till the time of use. Sometimes few constituents are higher in fresh plant material, which gets degraded after drying. In this case fresh plant material immediate after harvesting needs to be used for extraction or else needs to preserved so that active compound is not degraded till the time of use.
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I have to dry biological material to preserve it for late analyses. I first wanted to try a drying at 50 °C but finally chose at 40 °C to preserve the quality of sample. At 40 °C it will take longer, but does it have also an effect on the humidity of the sample at the end?
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Yes. The drying temperature has effect on water vapor pressure and in water activity of simple. At greater temperature, greater water vapor pressure and therefore lower water in sample at equilibrium. Your sample dried at 40oC has more equilibrium moisture (at end of drying) that your sample dried at 50oC. Exactly the equilibrium moisture (Xe) is the sample moisture (X) in which aw=(HR/100), where aw is sample water activity (aw=pvs/pvsat), HR is air relative moisture (HR=(pva/pvsat)x100), pvs water vapor partial pressure at sample surface, pvsat water saturation vapor pressure and pva water vapor partial pressure in air. At constant air moisture pva is constant, like pvsat(50oC)>pvsat(40oC) then HR(40oC)>HR(50oC) and Xe(40oC)>Xe(50o). If you want to predict the equilibrium moisture of your sample you need the sorption isotherm (aw=f(X)) of your sample at 40oC and 50oC and the drying air moisture (the pvsat can be easily found in water vapor tables).
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Is it better to explain fissure or crack generation during drying?
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Take a look at Feizollah Shabazi's papers
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The quantities will be low (~20 cc/min) but it is desired to maintain flow for long times (hours)
Ambient Conditions
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Hi Lampro,
Obivious you not usung nitrogen from cylinder, because gases from cylinders usually have very low humidity. Myabe your nitrogen gas source, is a nitrogen generator. So, if I assumed right, my suggestion is to order from Sigma Aldrich a tube with proper catalyst and with diamentions that are suitable for you (type of connections, flow values and percentage of humidity you want to vanish). There is a whole section at Aldrich cataloge that you can choose.
I wish to help you
Giannis
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I perform DSC,  temperature  -60 to 120C, of my spray dried powder sample. But i cant set the base line which transition 1 or 2  will be the glass transition temperature Tg. When i set to base line i got onset, endset and midpoint temperature. Which one is the Tg. In Gordon Taylor model,  Tg, Tgs, and Tgware the glass transition temperatures of the mixture, solids, and water, respectively,xw is the mass fraction of water, and k is the Gordon-Taylor parameter, how can i predict. specially k value . my sample solid about 96% water 4%. 
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Mr. Isalm-the first melting peak (1) is due to melting of ice crystal whereas second one is the Tg.You can find tons of work on milk powder by Bhesh Bhandari Group and Roos group.
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We don't have any device which is able to measure low air humidity values. Could anyone give a reference to published research concerning relative humidity over silica gel? How much water would contain a small aliquot of bacterial biomass desiccated for 2 weeks at 20°C?
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If air in the desiccator is removed through vacuum pump, regenerated silica gel (1200C for 2hr) can give about 7-9% RH. This is the result observed in my lab.
If air is not removed, initially RH in closed chamber depends on ambient RH. It takes longer time to reach equilibrium (RH 10%) and silica gel will also get deactivated faster.
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I can not trust to my calculations when APS has H2O.
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First of all: how wet is wet? A sludge? A wet-sugar type? - In any case no heat! I would place the mass of the salt onto wide Petri dish or watch glass and then in a vacuum dessicator with an Erlenmeyer flask half-filled with concentrated H2SO4. After 2-3 days it is usually stands at air-dried conditions. That means that your salt will not stick to a glass rod when you are mixing/shoveling it.   - Let me know how that goes...
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  Should respiration heat be considered as a factor affecting the vacuum drying process? The question is based on some experts' opinions on this effect.  
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I need to propose technologies for efficiently drying bagasse for experimentation in the industry.
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Mario,  we recently proposed a technology to a sugar producer in Asia a two fold process that would take both the bagase and vinasse from a sugar mill and convert it into biofuel, animal feed, chemicals and industrial fibers.  I have attached my engineers diagram of the process.  The ABE process was developed and used from World War l to the mid 50's.  The Managed Ecosystem Fermentation process is our and we are looking for partners.  The interesting point was we estimated the waste from the sugar mill is worth more that the sugar.
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The sample is supposed to dry completely prior to using FTIR  to see the spectrum without an effect of water. Ask
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Increasing temperature over 130oC it is no a good idea because the decomposition of organic material. Some degradation could occur also at lower temperature (100-110oC). For an advanced drying I suggest to use P2O5 under vacuum.  
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What is the most appropriate method to dry ethanol?
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Hi Charles.
Ethanol and water make an azeotropic mixture, i.e., is very difficult to completely separate the two components.
For instance, when you distill a mixture ethanol/water (e.g. wine), you'll never get ethanol 100% pure, even if you repeat the distillation many times.
To dry ethanol, means that you want to remove all water from the ethanol. You can do that by reverse osmosis, and repeat it many times.
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Why exactly? I have read that heating soils above 70 degrees C can cause some N compounds to volatilize, but I am having a hard time finding a reference to explain this. Is this 70 degree cut off the same for all soils?
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In general, yes, any heat above 70 (or even 65 Iʻve heard) can volatilize enough that it may affect the results. Even more so if you are going to examine N isotpoes. The 60-70 degrees C is pretty much the standard for drying all soils for total N analysis. the 105-110 degrees C is usually used only for when you are doing soil moisture.
A good resource for all soil methodology is:
Soil Survey Laboratory Staff. 1992. Soil survey laboratory methods manual. Soil Survey Investigations Report Number 42, Volume 2.0.
They donʻt talk about the reasons why so much, but this is one of the "bibles" of soil methodology. Always good to double check before you do analysis to make sure your methods are acceptable for publication.
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I am trying to understand the cost for drying of casein product. At present this material has a moisture content of 51% and expecting to get a moisture content <10%. I really appreciate your feedback and $/ton if possible. The method should be feasible for industrial production applications.
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This was my e-mail address, not the website.
I need to check this. Please give me few days for it.
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I am drying my enzyme a with freeze dryer with maltodextrin 0,5% as an additives. I did not get the fine powders shape, instead, I got sticky caramel-like shape. Can anyone here explain to me what is happening with my enzyme?
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You know the drying process used to removed the certain solvents from the sample. . The impurities attached to your enzyme may lead to this result. So you must be certain that your crude is pure. May be u make some mistake during the preparation process.
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I would like to calibrate a method to measure water content into concrete structure with TDR technique. My purpose is to monitor the weight of a 16cmx32cm concrete cylinder when drying. Because my TDR probe is rather large, I can not consider much smaller specimen. Of course, the hydric equilibrium will probably take a long time to be reached. I wonder if a moderate increase temperature (40 to 60°C) is a good way to speed up the drying process, because it may involve some water that would not have been released in standard (20°C) conditions. The calculation of water content could then be misleading. If somebody gets an advice or a comment, it would be very helpful for me. Thanks in advance.
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You can also try microwave curing for early setting and strength gain. Check the paper entitled "Use of microwave energy for accelerated curing of concrete: a review" by Makul N, Chatveera B, Ratanadecho P
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Keep constant frequency but various moisture contents
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temperature is constant but moisture is variuos. I had measured dielectric permittivity of wheat, maize and ... were temperature & moisture had changed.
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I am interested in performing a Lipid Extraction for MS analysis and the protocol states to dry the organic layer under a stream of N2 gas or speed vacuum. Is there a good alternative to this? The reason being, we do not own the equipment necessary to use N2 gas or a speed vacuum. Is there a cost efficient alternative?
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Hi, you can use any inert gas like N2, argon or others. You simply need a flue, a N2 gas bottle and a manometer. I think this is the most cost efficient method.