Science method

Desalination - Science method

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Hello every body,
Currently, I am working on a project focused on the fabrication of graphene oxide (GO)-based membranes. However, I have encountered an issue: I have been unable to produce a pure GO membrane. I am using a PES support without any cross-linker, but the GO layer peels off when I attempt to test its desalination performance. Could you kindly provide guidance on what might be going wrong?
Thank you for your time and assistance.
Best regards,
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You can deposit GO by vacuum-assisted filtration on a PTFE or PVDF filter and peel it off. It should be a couple of microns in thickness to be strong enough to handle.
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I dissolved the 5 Kg of sample in 40 liters of water and left it for 24 hours. Then I used a pump to collect the supernatant liquid without disturbing the sediment and then filtered it for any impurities.
I repeatedly evaporated half of the water(40->20->10->5) and decanted the solution after sedimentation with the help of a transfer pump four times. After that, with further evaporation followed by sedimentation, some grainy crystals of salt(table salt size) were formed, and the supernatant liquid was removed with the help of a pipette (filtration could not be done due to the viscosity of the solution). I found that this salt was KCl and it was present in good amount in the solution (though there could be other salts too) which made the resin salty (but the resin tastes bitter, not salty). In the end, I evaporated most of the water and kept the solution for 12 hours, small grainy crystals(smaller than table salt size) of KCl formed in the solution, and the consistency of the solution was such that the solution could flow slowly. Then I centrifuged the solution for 10 minutes at 1200 rpm in a 50 ml tube and found that the viscosity of the solution was low at the top and increased up to 15ml mark in the tube, after that the semi-hard settled salt present in the bottom of the tube. but the taste of the solution is still salty.
Is there any method by which we can completely remove the salt from the resin ?
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What are the new technologies for desalination and purification of seawater without the consumption of electricity that can already be applied in areas with freshwater scarcity?
But the scarcity of drinking water occurring in an increasing number of countries in Europe and also on other continents is caused not only by the progressive process of global warming, but also by unsustainable agriculture carried out in ignorance of the planet's climate and biosphere. But the scarcity of drinking water occurring in an increasing number of countries in Europe and also on other continents is caused not only by the progressive process of global warming, but also by unsustainable agriculture carried out in ignorance of the planet's climate and biosphere. The over-intensive, production-intensive cultivation of agricultural crops, mainly for the production of fodder for livestock rather than food for humans, and the production of exotic fruit sold mainly in supermarkets and hypermarkets in other countries, is also a significant factor in the excessive consumption of surface water and rainwater and the decline in drinking water levels over ever larger areas.
In view of the above, I address the following question to the esteemed community of scientists and researchers:
What are the new technologies for desalination and purification of seawater without the consumption of electricity that can already be applied in areas characterised by freshwater scarcity?
What do you think about this topic?
What is your opinion on this subject?
Please respond,
I invite you all to discuss,
Thank you very much,
Best wishes,
Dariusz Prokopowicz
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Fresh solutions to a briny problem
"Researchers are hunting for new ways to strip salt from water as the world’s freshwaters are becoming more salty and industries are producing more briny waste. Current methods are often energy-intensive or create problematic waste. Some scientists are using electricity to pull salt from water through specialized membranes. Others are working with a solvent that traps water — but not salt. With battery-makers clamouring for lithium-rich salts, future desalination companies could even turn a profit selling salts while offering clean water as a free byproduct..."
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Although there are several methods to obtain drinking water from the sea, it is quite expensive for agricultural use, which directly impacts people's living costs. This project introduces a new "Innovative Desalination Technology" to provide a cost-effective solution.
Research Proposal Seawater Desalination Plan
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undoubtedly man Farhad Vedad
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When comparing desalination technologies, it is useful to use total energy equivalent from thermal to electric energy. For example, one article I recently read states that it uses a conversion factor of 30%, but that is quite arbitrary.
I would like to know if there's a more formal methodology to calculate the total energy equivalent, because I also understand that there are losses between the power plants and desalination plants due to the electrical grid losses.
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We assessed the conversion efficiency of fuel to electrical power in various power generators with output capacities of 0.5 MWe to 1.5 MWe in 25+ industries and found efficiencies ranging from 25% to 40% according to the power generator design, its output capacity and its operating power.
40% is achieved by the best power generators with a capacity of at least 1 MWe and running at 80% to 100% of their capacity.
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Is it possible to design a membrane in the desalination device that does not reduce the salinity to the minimum possible level? Just lower the salinity to the level we set.
I mean we don't need to add some ions to the water again. Both in plant irrigation and in household desalination , where minerals are added to purified water.
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Thank you for your guidance
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With freshwater supplies under increasing strain, some have suggested utilizing desalination to provide water for agriculture. Desalination, the removal of salts from saline water to provide freshwater, could offer a drought-proof water source if scaled up significantly. However, desalination remains controversial due to its high costs and energy demands. I pose the question – should there be increased investment in desalination to supply water for agriculture?
Those in favor may argue that the technology has improved dramatically, leading to lower costs, and that combining desalination with renewable energy sources like solar or wind could reduce environmental impacts. Securing a reliable water source could allow expansion of agriculture and food production. However, critics note that even with technical advances, desalination remains energy intensive. The concentrate byproduct may also negatively impact marine ecosystems if not disposed of properly.
There are also concerns regarding how the high costs of desalination could affect food affordability and farmers' livelihoods. Careful consideration is needed regarding how increased desalination infrastructure would be financed. I welcome ideas on whether the benefits of supplementing freshwater with desalinated water for agriculture outweigh the costs and externalities. Please share your perspectives on the opportunities and challenges increased desalination could present.
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Increased investment in agricultural desalination should be done with caution, taking into account context-specific problems and opportunities. It may be a helpful solution in certain locations, particularly where water shortage is acute, but it should be part of a larger strategy that incorporates sustainable water management practices and takes environmental, economic, and social aspects into account.
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Hello
I am interested in understanding the applicability of gPROMS in simulating diverse hybrid desalination systems. Additionally, I want to explore the use of gPROMS for modeling Zero Liquid Discharge (ZLD) processes, considering its potential in assessing energetic, economic, and environmental aspects of ZLD systems.
Can you share insights into any existing dynamic simulations or models implemented using gPROMS for the stability and dynamics of desalination processes, particularly those related to ZLD options? Moreover, are there specific features in gPROMS that enhance its effectiveness in simulating hybrid systems with a focus on cleaner energy production, optimal energy management, and waste management? I would appreciate any expertise or experiences researchers may have in utilizing gPROMS for these purposes.
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Thank You for your guidance.
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Dear scientific community, Dear colleagues, Dear all. I have been contacted by many friends and family members from the Gaza Strip looking for any home-based solutions to improve the quality of the (little) available water in their households. The water that is still provided is highly saline (NaCl due to sea water intrusion), with high nitrate and microbial loads (due to sewage water infiltration). This is the only water available for hundreds of thousands among them. The UNRWA declared having no more fuel to supply the local small scale desalination plants and the population is left with this unique poor quality water for all life purposes. I adress this message to all the colleagues, friends, experts in all fields to provide, based on their areas of expertise, any solutions suggestions to help people, among whome hundreds of thousands of children, survive this catastrophic situation. All my gratitude to all of you in advance.
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Biodesalination is a concept that combines bioremediation and desalination processes to address water scarcity issues by removing salts and other contaminants from brackish or seawater. Traditional desalination methods, such as reverse osmosis, are energy-intensive and can have environmental impacts. Biodesalination aims to harness biological processes to make the desalination process more sustainable, eco-friendly, and cost-effective.
In biodesalination, biological organisms, such as certain types of bacteria, algae, or plants, are used to reduce the salinity of water. These organisms can either absorb salts directly from the water or facilitate the precipitation of salts, making it easier to separate them from the water. By leveraging the natural abilities of these organisms, biodesalination has the potential to reduce the energy requirements of desalination processes and minimize the environmental impact associated with conventional methods.
Research in the field of biodesalination is ongoing, focusing on identifying suitable biological agents, optimizing the conditions for their growth and salt removal abilities, and developing practical applications for large-scale desalination plants. The integration of biotechnology and desalination techniques holds promise for providing a sustainable solution to the global water scarcity challenge.
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Biodesalination is a promising sustainable practice, using lower energy consumption and resulting in less environmental impact. However, it is still in the research phase and has yet to be implemented on a large scale. Some challenges must be addressed before it can be considered a viable solution to global water scarcity. For example, biodesalination is slower than traditional desalination methods, and biodesalination costs are currently higher than other methods.
While biodesalination has the potential to be a viable solution to global water scarcity in the future, more research and development are needed to make it more efficient and cost-effective. Other methods, such as renewable-powered desalination, are also being explored as potential solutions.
See:
Can desalination be a sustainable solution to the water crisis? | World Economic Forum (weforum.org)
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In this article, they the used this equation CCe = (Fe*Pp*Np)+(Fe*PVp*nv)
to calculate the Elements capital cost in the pressure vessel for RO membrane.
(membrane + pressure vessels)
What is the corrective factor (Fe) in this equation?
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Anyone who is expert in Reverse Osmosis? I'm still looking for an answer.
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I am currently engaged in modeling the desalination performance of Cellulose Acetate (CA)/Graphene Oxide (GO)/POSS Mixed Matrix Membranes (MMMs) for reverse osmosis (RO) applications. The primary objective of my research is to develop a comprehensive understanding of the transport phenomena and rejection mechanisms within the membrane, utilizing the Donnan-Steric Pore Model (DSPM). As part of this endeavor, I am seeking to determine the effective membrane thickness.
During the membrane preparation process, I have acquired information that the solutions of composite membranes were cast onto a non-woven Hollytex polyester substrate taped to a clean glass plate with 250 μm thicknesses using casting knife. However, I am curious if there exists any way to determine the effective thickness of the membrane without resorting to experimental methods.
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Welcome dear Reihaneh.
Why not!
You can send me the SEM image and I will tell you the thickness. Be careful that the SEM image has to have a scale bar.
Best wishes
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Hi,
I was wondering if anyone had advice on desalinating LC-MS Metabolomics samples. We are studying the composition of uterine fluid which was collected by flushing with 50 mL PBS. I extracted the samples using methanol/ chloroform and dried them down. However, when resuspending the sample in water I read the osmolality of the sample and it was 4700 mOsm which will block the column and cause excess back pressure.
One of the key components we are looking at though are amino acids and all the desalinating columns I have been able to find will remove the amino acids due to their small size.
Does anyone have any advice on how I could desalt the samples without removing the amino acids and metabolites?
Thanks so much
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After taking some precautions and utilizing an ultra low-volume MS diverter valve in the flow-path, we routinely inject samples into our LC-MS system which may have some residual salts in the solution. *Ideally, samples should always be dissolved in the mobile phase, which in LC-MS analysis, should not contain any non-volatile additives such as PBS salts. In the case where residual salts or other undesirable materials remain in the injection solution, we develop the HPLC method to elute them at or near the column's void volume (Tzero) so we can redirect the column outlet flow directly to waste for a short period of time (often using a timed contact closure to the valve). Once all of the material (e.g. salts) has been safely eluted out of the column to waste, we switch the diverter valve back to the normal flow position to the detectors, restoring normal flow to the LC and MS detectors (in-line). Note: During the time in which the diverter valve is redirecting flow to waste, no liquid flow will be sent to the detectors. Lack of flow to the LC and esp. MS detector should be avoided. To maintain flow to the MS detector we us a secondary pump connected to the diverter valve's ports (an electronically operated, two-position, 6-port valve offers this option). The secondary pump is connected to the same mobile phase composition (same flow rate) as the main analysis uses. It automatically directs the liquid to the inline detectors when the diverter valve toggles to re-direct the main flow to waste. It then switches out of line when normal flow is restored (and the valve switches back). **This functionality is needed to prevent running the MS detector dry, resulting is HIGH noise and baseline disturbances (which may invalidate the analysis data and method). This is especially important if running in negative mode ESI (as an example) as source arcing may occur under conditions of low or no flow, damaging the needle.
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Capacitive deionization (CDI) is most known for its low cost and efficiency compared to other desalination technologies but has a downgrade in desalinating water when dealing with solutions with a TDS higher than 15,000 ppm as its pores start filling out with no space for other ions to be stored, so increasing the surface area should increase its pores size as well but what I am asking is about the technical reason itself why can't it desalinate higher TDS in addition to why is it not already done in real desalination plants.
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Hi Ahmed,
CDI, just like every other electrochemical/membrane based methods, is driven by ions transport. My thought is that if you have a higher concentration of salt in your feed solution than your rinse solution (recirculated on the electrode), you cannot accommodate much Na+ ions in your EDL after potential is applied. This can negatively impact your CDI performance.
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There are many processes. But overall which one is best ?
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To continue on the already explanatory answer given by Sergey Lvovich Gromov , productivity also comes into play. Some desalination systems are energy intensive. Those that are not energy intensive could have low throughputs. You could even find one with both energy-efficiency and high throughput but with high technoeconomical impact in the area of cost, etc.
In summary, there is no perfect system.
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Brackish water supply
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Hi dear friend
The desired area is in dry and desert conditions. The amount required is 40 Lit/s, for mining purposes.
Thank you
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What are best software for designing RO desalination systems?
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thanks for info
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what are best software for desinging RO desalination systems?
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Hello Abass, i couldnt find it in the web to download.
Even, It is Not on the official website.
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Are there any existing codes or software packages that can be utilized for this purpose? Any suggestions or guidance would be greatly appreciated.
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  1. Define the input parameters: MEDAD process requires input parameters such as the feed water flow rate, feed water temperature, and salinity of the feed water. You need to define these input parameters in your code.
  2. Define the MEDAD process model: The MEDAD process involves several steps, including multi-effect distillation, adsorption, and desalination. You need to define a mathematical model that describes the entire process.
  3. Implement the numerical method: Once you have defined the process model, you need to implement a numerical method to solve the model. There are several numerical methods available, such as finite difference method, finite element method, and finite volume method. You need to choose the appropriate method based on your requirements.
  4. Define the boundary conditions: The MEDAD process model requires boundary conditions, such as the temperature and salinity of the feed water and the product water. You need to define these boundary conditions in your code.
  5. Run the simulation: Once you have implemented the model and defined the boundary conditions, you can run the simulation to obtain the results.
  6. Analyze the results: After the simulation is complete, you need to analyze the results to determine the efficiency of the MEDAD process.
  7. Optimize the process: If the efficiency of the MEDAD process is not satisfactory, you need to optimize the process by adjusting the input parameters and repeating the simulation until the desired results are obtained.
In addition to these steps, you may need to consider additional factors such as the heat transfer mechanism, pressure drop, and energy consumption in your code. It is also important to validate your code against experimental data to ensure its accuracy. Good luck :)
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Hi all
Sometimes the flashing process are calculated with mass and balance equations like the following link:
But sometime the flashing process are calculated with "non equilibrium allowance"(NEA) like MED or MSF desalination
Why?
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I want a reference to cite please. I only found it in kWh/day.
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You should consider a range of values depending from size of the plant, salinity of raw seawater, and of course recovery ratio , use of brine rejects and finaly if you run the plant with energy from the grid or hybrid including renewable energy, solar mainly.
Current data are ranging from 2.7 to 10 kWh/m3 for the most efficient to the smallest ones not updated
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Hi everyone. I currently am working on a project about "capacitive deionization" for water desalination and I need to design an experimental cell. However, most manuscripts do not have an extensive details about their design an experiment. Can anyone here suggest me a paper or thesis with a thorough design please?
Thank you all in advance.
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How can I reach a sketch for the electrochemical cell (housing) of capacitive deionization? What manuscript I can use for that? Herbert Weidner
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I am going to work with spray flash desalination. I have a query related to the single droplet. How do I inject and generate a single droplet, e.g., for a micro droplet of 0.1mm?
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There are several methods that can be used to generate a single droplet of a specific size, such as a microdroplet of 0.1mm. Some common methods include:
  1. Capillary action: This method involves using a small capillary tube or needle to draw a small volume of liquid into the tube or needle and then release it. The size of the droplet that is generated can be controlled by the diameter of the tube or needle and the surface tension of the liquid.
  2. Electrostatic spraying: This method involves charging the droplets of liquid as they are expelled from a spray nozzle using an electric field. The charged droplets can then be attracted to a grounded target, allowing for precise control of the droplet size and location.
  3. Microfluidic devices: These devices use small channels and pump to precisely control the flow of liquids, allowing for the generation of very small droplets.
  4. Laser-induced breakdown: This method involves using a laser to vaporize a small volume of liquid, which then condenses into a droplet. This method can be used to generate very small droplets with high accuracy and control.
Each of these methods has its own advantages and disadvantages, and the most appropriate method will depend on the specific requirements of your application. It is important to carefully consider the factors that will influence the size and stability of the droplets, such as the properties of the liquid, the operating conditions, and the desired droplet size and precision.
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I have to take decisions about some activities in marine protected areas - what level protection are we providing if these activities are occurring?
I am looking for any good references on the impact of:
- desalinization plants: its construction will have severe effects, then it seems like the brine should not have a very important impact (salinity in liveable thresholds), but seems there are always some metal pollution, any idea of its impact? what about the water extraction?
- geothermal extraction: same the construction will have a lot of impacts, but once it's built, i have only found info on its carbon footprint. Are there other impacts, pollutions?
Thanks to everyone that have an idea to share with references 🙏🙏
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Looking at your question about geothermal impacts more closely - I am not sure if you are looking specifically at impacts on the marine environment or impact in general. The environmental impact of a geothermal power plant depends on the type of plant being used, Binary power plants use a heat exchanger and the produced geothermal brines are generally all reinjected so there is virtually no interaction between the produced fluids and the environment aside from heat transfer to a secondary fluid to generate steam to drive the turbine. More conventional high temperature flash plants use steam produced from the sub-surface directly to spin the turbines and these fluids can contain things like sulphur and nitrogen compounds that have negative environmental impacts. However, unless a geothermal plant is located adjacent to the coast I would not expect any significant effects on the marine environment, although some could occur.
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Hello, is it possible to purchase this article,
Analysis of energy usage at membrane water treatment plants, Desalination and Water Treatment, 29:1-3, 63-72, DOI: 10.5004/dwt.2011.2988, R. Singh
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Thank you Bestani. I was under a time crunch so I found a way to purchase the article. I appreciate you getting back to me but I'm all set.
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Is there any microbe that uses and changes salt? (not just tolerate)
Can we use microbes in desalination?
#salt #desalination #Halophile
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Dear Zohre,
I would suggest listening to this TED talk (3 minutes)
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Hi, I have conducted membrane performance tests using MD (8 hours) for desalination application. Water flux always fluctuates in the early stage of the performance, usually in the first two hours before it increases. My membrane material is a modified metal-organic framework on alumina substrate.
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noted and thank you so much Tijjani El-badawy
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Hello, Please I am looking for a file that collects the characteristics of different composite membranes used in desalination.
Thank you.
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Good day! I suppose they do not exist in free market. The easiest way is to compare membranes by different producers.
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In many papers, the flowrate determination has been given as the Bernoulli equation for the determination of brine flowrate however the equation does not remain valid for the last effect because the amount of brine getting out of the last effect gets increased because of this. This is needed for the dynamic simulation of multi-effective desalination systems.
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The Bernoulli equation is only valid for a limited subset of problems. Many people don't realize that the Bernoulli equation applies along a single streamline, not across multiple streamlines, which also means that it doesn't apply across phase boundaries or changes in composition. This does not mean, however, that you can't use lumped system analysis and obtain quite accurate results. Google "Crane Technical Paper 410: Flow of Fluids through Valves, Fittings, and Pipes." I was part of a Team that developed the first pipe network solving software to ever meet the stringent quality assurance requirements of the NRC. This type of system (dynamic brine desalination) can be solved but it will take more than the Bernoulli equation and even if you use some commercial code, it will require significant effort.
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So what is the factor effect in salt rejection? What is the expected explanation?
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Can you provide us the information about your membrane?
what types of membrane it is?
Also the rejection depends on nature and concentration of salts.
Thank you.
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Hi, I am new to comsol Multiphysics, I have an electrodialysis model, I add a separator as an ultrafiltration membrane but it doesn't show any separation in the process. I am doing some mistakes if anyone can help me I will be very thankful to him/her.
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Electrodialysis is a separation process for electrolytes based on the use of electric fields and ion selective membranes. Some common applications of the electrodialysis process are: Desalination of process streams, effluents, and drinking water. Electrodialysis with inserted ultrafiltration membranes is an alternative method of peptide separation into fractions, their concentration and possibly demineralization at the same time to achieve large production quantities.
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Hello, esteemed researcher If you have recent literature regarding understanding desalination, please share it with me.
Thank you
Dr. Vinaya
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Thank you Arvind Singh Sir
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How we can evaluate different desalination processes when they use different form of energies such as electricity, steam, renewable etc...
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In terms of studying about different desalination technologies, I would recommend the following research article:
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I have found two articles in which the correlation is explained but are equivocal. The first one is about spacers and the second one is about woven mesh backings. In the first reference, the maximum stress is formulated to be proportional to the square of pressure difference, while in the second one it has linear relation with pressure difference:
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Ali Naderi Beni I recommend you to go through the following theoretical studies.
These works would give you clues about what you want to know.
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Recently I am working on desalination project . So I need to recent desalination project going on india.
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Dear Satyabhanu Behera,
You are welcome.
Regards
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For water treatment (say desalination for example), the charge of any saline solution should be neutral. Analyzing the water via IC and ICP will provide concentrations of anions and cations, which can then be used to calculate milliequivalents per liter.
To calculate the charge balance I have seen equations that state:
[SUM(anions) - SUM(cations)] / [SUM(anions) + SUM(cations)] in meq/L
My question is, why is the denominator taken as the sum of the collective anions and cations? Why not the average of the anions and cations?
Thanks in advance!
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I did have this concern as well. Most people give this the same equations,
[SUM(anions) - SUM(cations)] / [SUM(anions) + SUM(cations)] in meq/L
But I feel it doesn't make any sense for me.
Fortunately, I found this link
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How can I determine the vacuum index of the membrane used for desalination?
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Dear Kien Vu,
On which page of the article the vacuum index of the membrane is mentioned? Thank you.
Regards
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The unavailability of this software makes me difficult to design this system.
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You can try the PVsyst software:
Regards,
K
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What is the difference between active desalination and inactive desalination?
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Today there are two main types of desalination technologies – membrane (RO) and thermal (MED, MVC and MSF) desalination. Reverse Osmosis (RO) desalination uses the principle of osmosis to remove salt and other impurities, by transferring water through a series of semi-permeable membranes.
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These days, the more technology is growing, the more experts work on greenways to desalinate seawater to produce drinking water. One of the most notable of them is undoubtedly solar desalination.
But, besides a lot of advantages of the solar method, there are weak points that prevent this technology from maturing compared to conventional methods such as electrical energy, fossil fuel, etc.
Please give your idea and thoughts about these limitations.
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People have strong opposing views against solar desalination due to following reasons:
  • Solar plants and solar desalination process are expensive
  • It requires a lot of energy to process which could also lead to environmental impacts
  • It is a passive contributor for global GHG emissions
  • The resulting brine would contaminate the environmental water bodies and lead to the destruction of aquatic species
  • Solar desalination requires highly skilled professionals.
For more clarifications, feel free to contact me @shuraik10@gmail.com
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Hi,
I am going to measure antiscalant in brine of a desalination plant. According to the information provided by supplier I have to determine the amount of carboxylic acid. where can I find the protocol?
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To determine the concentration carboxylic acid dissolve it about 0.3 to 0.4g.in 250 ml of ethanol(96% and dilute it in a volumetric flask. Titrate aliquot of solution (25ml)against standard alkali aq. NaOH (0.1N )using phenolphthalein as an indicator just like acid base titration. Following relation will be useful for determination of the conc. of an acid.
1000 ml of 1N NaOH requires ......g.equivalent of acid for neutralization ,then
,x, ml of 0.1N NaOH will require ....g. of an acid
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Solar Multi Effect Distillation (MED) and Multi Stage Flash Distillation (MSF,) though appearing to be natural and tempting solutions, cannot be taken as proven technologies. More and more developments in both solar power and desalination technologies are expected to keep these solutions competitive compared to Reverse Osmosis (RO) systems coupled with conventional power plant. Somewhere, solution lies in combination: combination of heat sources and combination of processes. Recent developments present desalination systems including MSF combined with reverse osmosis, heat source being a thermal power plant, but coupling with solar resource can be imagined Main advantage of that installation is that RO can run during night times when electricity costs are low and MSF work during daytime with low running costs due to low pressure steam. Water storage offers flexible solution with energy consumption optimized. Addition of solar energy from start of the project (with parabolic troughs) would have low cost impact but no GHG emissions. We can note that the range of possibilities is widely open in desalination. Need for fresh water will always be present, therefore desalination technologies must be enhanced to become cleaner, more efficient and more virtuous.
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Hello Ahmed Sir,
Excluding Reverse osmosis, the most competent to this technology is "Electrodialysis ". There are other techniques as well like Membrane capacitive de-ionization (MCDI) , thermal based processes, etc. However, considering the energy consumption and TDS removal aspectes, ED out performs the MCDI. For energy requirements the input energy can be taken from Solar panel powered grids.
So such hybrid systems are potential alternative to resolve water crisis issues, still the scientific communities are trying to reduce the size by engineer aspects.
You can also refer to our groups work on Brackish water desalination via Electrodialysis. In recent work we also validated that applying an optimized potential, the bacterial contaminations in crude ground/brackish water can be reduced by 99%.
Here I am attaching the links of some crucial papers for your kind persual.
1.ED outperforms MCDI
2. Potential optimization for pathogen removal
3. Electrodialysis over other desalination techniques
Attaching one PDF file as well. In introduction you might get some information.
I hope it will help you query
Regards
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I design a plant for producing caustic soda and chlorine from electrolysis of brine (salt from desalination plants)
How can i use aspen plus in simulate the electro chemical cell (membrane cell) •??
📷
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You can read this paper:
Aspen Plus model of an alkaline electrolysis system for hydrogen production
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I have a 50uL solution and I need to remove salts from the solution, how would I go about doing so? 
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You can use nanofiltration membrane for your solution
Regards,
K
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To increase the water recovery in RO desalination units, one is to use counterflow RO units, which use osmotic mediation to decrease the required hydraulic pressure. One of the points about them is that it's better to have equal flow rate on low and high pressure sides. Is there any reason beneath it?
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I need to monitor all kinds of fouling (colloidal, organic, scaling, biofouling) on the reverse osmosis membrane in the desalination process. what are the practical (easy and reliable) techniques used to monitor (or visualise) these types of fouling?
and what are the settings used to have fouling layer development on a membrane (feed flowrate, membrane surface, feed type, etc...)?
thank you?
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Abdeljalil Chougradi i found two interesting papers on the same topics and felt like sharing with you and hope so it is of your interest as well
This shows the review of the fouling indices and monitoring techniques for Reverse Osmosis
second one is the
this is about the fouling control in Reverse Osmosis
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What are the best technologies used to desalinate water on a large scale using solar energy, and how practical are these technologies?
knowing that the source water is not marine water, but rather water taken from rivers and sewers with salinity slightly more than the permissible level.
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Thaer Roomi i came across one paper and felt it interesting and it was regarding the desalination using solar radiation and I thought might be of your use as well am sharing the link here with for your reference
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The problem of the demand for fresh water is greatly exacerbated by the increasing consumption of water as a result of the increase in human population growth around the world on the one hand, and the persistence of the problem of climate change and global warming on the other hand. We do not want to talk about international problems and the possibility of wars due to the conflict over water in the riparian countries on the rivers, but we are talking about air pollution. Building more desalination plants leads to the release of larger quantities of toxic and greenhouse gases such as carbon dioxide, nitrogen dioxide, sulfur dioxide, etc. Are there solutions to control pollutants, or are there desalination plants that do not use fossil fuels?
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Thanks again and again for your valuable answers.
The Arabian Gulf countries use the desalination plants, which is more fast and efficient than the rest methods. Even the distillation technique needs a lot of efforts and people to run it, the matter that make the first technique is more reliable but with environmental risks.
Regards
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I am graduate student working on an independent study related to solar desalination. While I am conducting my research on the costs involved and the challenges faced, I wanted to reach out on this forum and see if I can get some inputs on how solar desalination can be made cheaper. Any feedback will be appreciated.
Thanks!
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Insulation is required to keep the thermal energy inside plus you have to use mirrors in the interior to reflect the solar energy
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First of all, our destinies are all in the hands of Alla Almighty.
In the field of scientific research, the desalination processes of the seawater "desalt seawater" is very essential to have enough water in the world for the coming years. This technology may help to overcome the expected water shortage in the coming years.
All comments and contributions are welcome
Thank you very much.
My Best Greetings.
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Actualmente extste la tecnología necesaria para la salinización del agua y convertir el agua salada en agua potable. Este proceso es importante porque el mundo está rodado de mares y océanos y las reservas de agua dulce cada vez son menos y el agua se necesita para la vida en la tierra
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Graphene, Desalination
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https://www.nature.com/articles/s41545-018-0004-z - Outlook for graphene-based desalination membranes
Graphene membranes for water desalination
Few of the links shared which i felt was usefull for you and hope so this will answer your question
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We are launching a Ph.D. research looking at the effect of salinity and temperate increase on the bioerosion rates in coral reefs in the northern Persian Gulf. In doing so, artificial and natural blocks will be submerged along a gradient of salinity and temperature where hypersaline water from the desalination plant discharges into the sea. We are planning to use two types of natural and artificial blocks including (1) natural blocks by segmenting dead massive corals (e.g., Platygyra sp.); and (2) artificial blocks made of carbonate calcium.
But wonder how to make artificial blocks that need to be identical to natural blocks in terms of porosity and texture. Can we use crushed dead corals that have been blocked by a glue? If yes? What type of glue?
Wondering if anyone has experience in making such artificial blocks.
Best regards
Mohammad
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Agree with Mr. António Godinho.
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As water means life, and under the worse circumstances of gradual scarcity of water resources, desalination technology has became urgent to be applied on a wide range than any other time of the past. Therefore, I open the topic to have feedback of the modern desalination technologies and solutions.
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Desalination is the solution for water scarcity in the world but it is expensive. It depends on energy use. Renewable energy (solar, wind) can be used especially if it is available in the country. Desalination Integration with Renewable energy can be used as in the link:
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I am trying to analyze cost of desalinated water (LCOW) collectively for a few regions in California using a solar desalination technology. Treating this as a system to be actually producing water for real consumption, I would like to apply all possible incentives such as rebates, tax credits or tax deductions and any other incentive available at state and federal level, as a public utility (small scale desalination plant <100 m3/day).
I found 20% rebates for solar thermal technology and solar PV but nothing on solar / renewable desalination plant. Can anyone please share available materials that I can add to cost models for more accurate picture of cost of water produced?
Thank you.
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All the best
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I want to know how I can prepare a composite membrane with uniform pores to separate sea water(water desalination).
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You can check the paper below for the answer:
Good luck!
K
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My research is about solar membrane distillation for desalination systems. I'm trying to use Trnsys and Aspen Plus softwares, but I don't know how i can link these two software. Is there anyone who can help me?
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Hey Marziye!
Did you find the solution of linking Aspen Plus with Trnsys software. I am facing the same problem.
Please let me know the tool used for integrating Aspen Plus and Trnsys.
Thank you
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On the surface of the planet Mars are the basic components, organic elements and chemical compounds necessary for the cultivation of terrestrial plants on Mars.
There is water on Mars (saline, it would have to be desalinated) and on the surface of Mars there are elements necessary for the development and cultivation of plants.
There is, however, no atmosphere with the right composition for the earth's plants, which could possibly be cultivated in the future on Mars.
In the next few decades, will human civilization reach such a level of technological development that Mars should begin to grow plants and begin to colonize Mars by building specific stations and cosmic bases there?
In the light of the above, encouraging discussion, I turn to you with the following question: What technologies should be developed on Mars so that plants could be grown on Mars in the future?
Please, answer, comments. I invite you to the discussion.
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All the conditions necessary for plant survival should be created in Mars.
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I am planning to build a thermal ZLD pilot to separate salt from the effluent of desalination systems. Includes evaporator and crystallizer
I would be very happy if any experts with experience in this field would share with me. Especially the metal material in the parts that are directly exposed to high-temperature saltwater and the type of coating is very important to me. Of course, if you have an opinion about the proposed capacity of the pilot, please let me know. The specification table of the desired effluent that will be the input of this pilot is as follows.
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Abbas Akbarzadeh You can find some information about the design of a ZLD system at
There are also some data about construction materials of crystallizers in
Industrial Crystallization (Process Simulation Analysis and Design) by Narayan S. Tavare, Springer-Verlag.
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Dear Researchers
I am pleased to share with you this online training module about Water Desalination.
Desalinated water is a fast-growing demand that exceeded the production of 100 million m3/day and distributed globally in more than 100 countries, especially in the Middle East and North America.
This course helps you gain insights into desalination in terms of desalination statistics in the world, water chemistry, desalination technologies, desalination economics, and other fruitful information with plenty of associated documents.
This course discusses multiple technologies including thermal desalination (MSF, MED, VC), membrane desalination (RO), solar desalination, ion exchange desalination, and others.
Hope you enjoy this course and find it fruitful to build or strengthen your knowledge in this promising multidisciplinary field.
The course link ..
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Hello
Yes of course. I can give you a 90% discount for students. If there are many students, the lecturer or teacher will be given a free access and will be getting 90% discount for his students.
If it is okay, contact me through private messages.
Regards
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I am trying to assess the sustainability of a floating desalination platform and I am looking for a solid methodology to assess the whole project consisting of a hybrid solar/wind power system, Reverse osmosis desalination plant and an offshore platform.
Any recommendations?
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Desalination plants are often coupled with a water storage tank to mitigate demand/supply fluctuations. What is a good assumption for the capital cost of such a tank in "Dollar per volume". The number should be valid for tanks with a volume > 1000 cubicmeter. A scientific reference supporting the answer would be great.
Thank you all!
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citation of the paper is
Clement Kiprotich Kiptum , Steve Ochieng Ochieng , Victor Muroki Mwirigi, 2020, Cost and Waste Evaluation of Expanded Polystyrene (EPS) Model House in Kenya, INTERNATIONAL JOURNAL OF ENGINEERING RESEARCH & TECHNOLOGY (IJERT) Volume 09, Issue 07 (July 2020),
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In some lower sahara regions groundwater salinity increases continuously where it sometimes reaches 4 times more than the WHO standard for drinking water. We can do desalination treatment. Is there other way toreduce the water salinity? are there some actions done in this field? Thanks
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In the Desalination Pretreatment Facility, what is the mechanism and chemical reagents used in Dissolved Air Flotation as pretreatment of water?
#DAF #RO #Water #Desalination #pretreatment #membrane
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Here in the link you can find also a good overview about SWRO-Preatretment systems (incl. DAF).
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jelly fish ingress is a major problem affecting the sea water intake systems leading to plant outages in power plants and desalination plants. can anyone through some insight on installed and convinced jelly fish ingress preventions solution...
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There are many regulations, depending on where you are at (or where your project will be).
Planning stage:
A basic minimum is to review existing data that will help identify species their life stage in the area where you are considering the intake. Quantify their relative and peak abundance, identify what is most susceptible to impingement and get an operation and maintenance (as well as some QA/QC standards to revisit the data and analyze it.
Design/Construction/Operation:
-Regulations in the US can be found at https://www.epa.gov/npdes
-Impingement and entrainment sampling. A must.
-Quality of water (including effluent): Temperature extremes and low DO usually impacts marine life and keep them away from the intake.
-More on water quality: Jellyfish and algae have a symbiotic relationship. Jellyfish swims in stagnant (or semi-stagnant) coastal conditions to ascertain that algae receives sufficient sunlight for the photosynthesis process. In return, algae gives the jellyfish nutrients and energy. On the other hand, the survival of marine life depends on a sufficient level of DO. Low DO takes place because of excessive algae growth caused by phosphorus and nitrogen (nutrients that can contribute to algal growth). As algae die and decompose, the process consumes DO and makes marine life challenging. So, it is important to construct your SWRO in areas with low algae growth.
-Intake location: An intake in a biologically productive area creates a greater risk of exposing marine life to the intake system. Select a location where minimal biological activities are present.
-System hydraulics: An intake at a semi-stagnant area is an invitation to a risky and potentially harmful operation to marine life. Consider placing your intake at a location with relatively strong ambient currents. This will push jellyfish away.
-Avoid active intake screening systems that collect and return species to the coastal waters. Passive intake screening systems seem to work better.
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Hello colleagues, I am currently working on solar desalination experiments. I have to find the optimum angle at which my solar still gives maximum performance. But I only have two solar stills and have to rely on solar radiation for the project. At a time, I can only compare two angles per day, and also the solar radiation is not the same every day. Is there a method or analytics with which I can compare the angles of the system reliably.
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Thank you all for your answers as it has been really helpful for my project.
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Designing a desalination reverse osmosis membrane system. Could someone recommend me some designing publications or a step by step calculation guide for the design? Much appreciate.
Thanks :)
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They are a lot of free design tools like "WAVE", "LewaPlus2", "TorayDS2", "WinFlows 3.3.3", but if you look for some practical recommendation for the design you will find something on the following page: http://wagnerdk.dk/DownLoads.htm
Especially the "Membrane Filtration Handbook" is not up-to-date but very good explained. You can download there also other interesting articles and calculations.
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Hi world, I'm curious about whether having to put nanofiltration on the first phase then reverse osmosis on the second phase to desalt seawater that has a roughly 35000ppm of TDS will lower down the pressure requirement of the RO process or the overall energy requirement of whole process?
Since after NF, the TDS in seawater will be lowered and during RO process less pressure will be require to turn the seawater (after NF stage) into drinkable water. Does this actually work in terms of having a lower energy requirement in the overall process?
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NF+RO combination is capable to improve RO sustainability in sea water desalination applications. Due to the options of Hardness and TDS partial removal, organics and some other contaminants rejection at NF step. So RO could operate in a "softer" conditions and RO recovery could be increased. Some savings should be associated with RO permeate flow increase and RO maintenance costs reduction (in case of NF+RO). But power consumption is an issue that needs to be checked case by case. Although Weak Acid Cation in front of RO will bring you energy costs reduction for sure.
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I want to compare various desalination methods. Which model should I adopt to compare them?
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Abhijeet Singh No but I want to write the same answer in order to help him to clarify his question that why I wrote the answer
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I'm Director of Research & Development for a company that specializes in new Alternatives, Exotic and/or Green Technologies for use in Environmental Remediation, Alternative Energies, Waste-to-Energy, Compost/Biogas, Oil Spill Recovery, Water Generation (desalination alternatives) and Protective Materials for Nuclear Fallout and Contamination. Clean Nature Solutions (thecnsgroup(dot)eu) is looking for the latest technologies to help promote and utilize in various projects World Wide. Please contact me if you have something unique.
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Most probably degenerate parametric amplification circuits are what you are looking for.
Unfortunally for you, USA and Soviet applications are secreted, and control of energy produced by these as well.
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Oil contamination is a major issue due to spillage, transportation, dumping etc. How much it impact on desalination process/plant. What are the techniques that can be employed to avoid the impact of oil contamination in desalination plants?
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Many thanks Augustine for your input.
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SDI indicates the fouling tendency of membrane. Is there a possibility to relate the TOC of saline water to SDI so as to measure indirectly the fouling tendency of membrane in RO desalination systems? Would like to see any reference related to this concept!
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Generally SDI of seawater is less than 5, maybe total carbon can relate to it rather than TOC alone.
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Hi world, I'm currently doing a research for my final year project. And currently I'm having trouble in looking for a transport model for COMSOL regarding a reverse osmosis desalination membrane.
Could any kind soul please help me with this? It will be greatly appreciated.
Thanks :)
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Hi Hock Chee Lu,
I think this article may help you a lot. Here, Molecular transport through a single nanopore in lipid membranes of vesicle has here been studied by COMSOL simulation
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The environmental impacts of all desalination technologies, whether in use or under development, must be considered.
My question : which environmental aspect is s to consider in a seawater desalination project?
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Aside from the general impacts of construction and long term operation of an industrial scale facility, the major issue associated with desalination is brine handling, either through discharge or reuse as brine.
If discharged it must be diffused to dilute it so as to not cause adverse effects in the zone of mixing.
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What is the best technique to desalinate sea water based on cost and environmental consideration?
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Dear Gamal B. Abdelaziz,
there is no unambiguous answer to your question, because cost and environmental considerations are determined by the local conditions and regulation in each case.
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Is Solar water desalination Operates on the daylight only? Can it operates after sunset? Can it produce pure water on the midnight for example?
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If you want to continue desalination during night then the most feasible option is hybrid system.
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ISSN Print 1944-3994, ISSN Online 1944-3986
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Source title : Desalination and Water Treatment
CiteScore: 2.7
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In solar desalination still, the water is heated by the absorbed solar energy. At some point, the temperature in the still reaches the boiling temperature. I would like to understand the mechanisms within this process and find out how to calculate the mass transfer.
For non-boiling temperature, I normally use the analogy between heat and mass transfer to calculate the mass transfer. With Sherwood number, we can approximate the convective mass transfer from the diffusive mass transfer, with a Sherwood number obtained from the Schmidt number and Grashof/Reynolds number from heater transfer. But if the water is boiling, the turbulence within the water kind of breaking the laminar boundary assumption used in diffusion theory. In this case, what is the dominant mechanism in the mass transfer? How to calculate the mass transfer?
Any discussion is welcome!
Thanks
Wenlong Chen
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Specific heat has to be computed along with input of othr parameters to decide
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I got the idea from using filters and other filtration systems in previous research experiences, and also how recently... someone gave me a bunch of Monster Energy drinks but they aren't sugar free so it got me thinking how it would be possible to extract the sugar from the Energy Drinks mechanically.
Sugar molecules are 1nm in size
salt (NaCl) is .06nm in size and water molecules are .275nm in size.
Would this work as planned or is there something my reasoning has a huge gap in? :)
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Not possible it is in dissolved state. You need to use evaporative crystallizer
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I am doing a small research to review the water related open source tools / software (e.g FREEWAT).
if you have used/developed/ heard of similar tools,please share it with me ?
Thanks in advance
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Yes USGS based softwares eg MODFLOW, Modelmuse, mt3dms, modpath. check their website for more info. All softwares are free and open source
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what are the advantages of using renewable energies for the desalination of seawater?
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The origin and continuation of mankind is based on water and energy that always control the growth and development of human societies. Climate change, increasing urban population and industrialization have increased the demand for fresh water worldwide. However, about 97% of the earth's water is salt water in the oceans, and a tiny 3% is fresh water. It is estimated that a small percentage of all freshwater produced in the world comes from renewable sources. Through technology development, lower equipment prices and increased attention to the environmental problems of fossil fuels, renewable energy is increasingly being used. In some cases, concentrated solar energy can be used for thermal desalination or electricity generated from solar power stations for membrane desalination systems in arid regions. See, for instance, the attached file:
Article Seawater desalination using renewable energy source /
  • DOI: 10.1016/j.pecs.2005.03.001
Book
Seawater Desalination: Conventional and Renewable Energy Processes
  • DOI: 10.1007/978-3-642-01150-4
Article Hybrid renewable energy systems for desalination
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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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There are many types of water desalination plants; Reverse Osmosis, MSF, Solar desalination units, ........... etc.
How much water does each desalination plant type produce and what is the approximate inertial capital cost and running cost of each system per 1 liter of pure water?
Thanks
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Mostafa Ansari Thanks a lot
Please send me the economic analysis
I am really interested
Thank You
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I want to find the energy consumption per unit volume during a waste water treatment processes. It should be comparable and also according to the pollutants concentrations.
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Use Bernouli.s equation and data from membrane manufactureres.
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I'm studying the fouling of RO membrane for desalination of seawater or brackich water. what is the minimal concentration of foulants (inorganic salts, organic foulants) in feed water which would allow the formation of fouling layer in less than hours ? and at what flowrate should I set the feed pump ?
Best regards.
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Is there any difference between in the efficiency of graphene oxide and reduced graphene oxide in water desalination?
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Hello! It depends on the extraction process and type of pollutants, on functionalization to reduce GO, PRODUCTION ERRORS AND COST. It is difficult to say without evaluating the process as a whole, because the layer structure is dependent on the go production process, functionalization and membrane production process. For use in membranes, you will need to functionalize the structure.
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I am building a solar desalination still and the inside glass temperature is required for the condition whether the glass has attained the dew point temperature of the vapor inside the still. I am using a thermocouple that is stuck on the glass using a transparent tape inorder to reduce the opaqueness of the object. But the radiation falling on the thermocouple increases its temperature than the glass temperature. I would like an alternative approach without this problem.
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I agree with Mr. Edwin
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Dear sisters and brothers,
I am wondering if anybody has performed experimental work to desalinate high brine concentration of with 60 kg/m3 using spiral wound Reverse Osmosis process and if that was practically afforded or not considering fouling issues. Any guidance for such published research would be highly appreciated.
Hopefully, this question would open the doors to limit the disposing of high concentration brine into the water bodies.
Regards
Dr. Mudhar Al-Obaidi
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Thank you Mr. Ahmed
I agree that high pressure RO process is required to manage high concentration brine ...However, I still looking at any actual experimental work for this purpose
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Greetings dear colleagues.
Is there any formula or method, to estimate the salinity of the desalinated water output of a RO (or other system) desalination system? For example if you have 100 m3 of a water with salinity of 10 ds/m, what would be the salinity of the water output? and its volume? what would be the salinity of the brine? and its volume?
Thank you
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If this is not for academic purposes, you can use also try out the freely available simulation softwares from membrane manufacturers. DuPont (formerly DOW Water) have a simulation program (WAVE) where you feed in your raw water quality and % recovery, and it models for you the permeate and brine qualities expected. The software is available for download on their website and it's prediction ability is quite good having used it to build RO plants
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DEAR TEAM MEMBER
i am intrested to know the necessary laboratory tests required for the assisment of the existing concrete structure which is around 35 yrs old and is still existing and in use.
We are intrested to used the same intake structure as source of intake of water prior to desalinate.
Accordingly am intrested to know the requird important tests that neet to be conducted on the existing concrete structure prior to decide that it will serve the need or not for the construction of new RO plant
Please advise
Regards.
Nisar Ahmad
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You can make use of several NDT tests depending upon the type of information you are trying to seek. In water storage it may be corrosion and in other structures it may be strength. There are other models to predict service life of structures depending upon the current damage assessment.
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a water desalination system depends on humidification between air and hot sea water to be desalinated from salts and the hot moist air should be condensed to collect fresh water, could honeycomb and venture tube condense the moist air to separate water droplets from air? would it be effective?
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Is it possible that the desalination processes are environmentally green and have you heard about the experience of any country?
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Very attractive discussions. following.
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Is it possible for desalination plants to be environmentally friendly and reduce environmental pollution
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Yes, it can be done and if it is successfully transferred to field, it will be a breakthrough to phytoremediation research. But the genuine problem is- How can you proceed towards desalination of plants? Do you have any standard protocols?
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Dear scholars,
I'm working on a project that uses some waste heat to provide the motive steam for multi-effect desalination with the thermal compressor.
Pressure, Temperature, and flow rate of the motive steam are known. I need to calculate the amount of salt-free water and detailed state of the effects.
I would appreciate if anyone can help me with Matlab or EES code.
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Membrane fouling is a process whereby a solution or a particles are deposited on a membrane surface or in membrane pores in a processes such as in a membrane bioreactor, reverse osmosis, forward osmosis, membrane distillation, ultrafiltration, microfiltration, or nanofiltration so that the membrane's performance is degraded. Membrane fouling is thea major obstacle to the widespread use of this technology.
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Dear Ronei de Almeida thanks for your detailed answer and contribution in the discussion.
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I am working on design of desalination plant, and we are modeling a desalination process using RO. The process has sea water entering and brine, desalinated water exiting. The problem with modeling we are facing is, we need 2 property methods at once. Our input water has suspended sand particle and electrolytes Na+ and Cl-. There are 2 different methods for modeling electrolytes (ELECNRTL) and solids (SOLID).
So should I create two model files, one having pre-processing of sea water for removal of suspended particles and 2nd for RO plant? It does not sound a good approach. Would be happy to hear of any other possible way to model it (preferably in Aspen Plus).
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You can use a hierarchy for each part of your process where you need to use a different method.
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97% of earth surface is covered by saline water in the form of ocean and sea while only 2.5% as fresh water.
If fully utilized then there will be no hungry soul on this earth struggling hard for water.
How can such be possible with low cost and with maximum durability
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We talk about cost only when we have alternatives. With time, without alternative, cost may be neglected.
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feed water in MED Technology for desalination water have to have charactrization . for examel What is the maximum BOD and COD of feed water in MED? mybe destroy pipes in MED
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NO LIMIT, BUT YOU HAVE INSTALL STRIPPER OR COLUNMS TO REMOVE OR RECOVER LOW BOILER SOLVENT FROM THE EFFLUENT BEFORE FEEDING IT TO MED.
YOU HAVE HAVE INORGANIC SALT AND THE SOLUBILITY OF THE SALT AT RESPECTIVE TEMPERATURE AT WHICH YOU ARE OPERATING THE MED IF YOU ARE GOING FOR ZERO DISCHARGE.
FOR FURTHER DETAILS YOU CAN CALL ME ON 0919904001159
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Desalination of salty groundwater and seawater could unlock the vast water resource and provide a sustainable source of water to water-stressed regions of the world. Desalination processes have been categorized into three main areas: i) thermal or phase change processes, ii) filtration-membrane processes and iii) intensified processes which involve integration of various processes (Gude et al., 2010). However, these methods are costly.
Objectives our project are as follows:
1: To introduce an economic and viable system to the desalinated ground-waters in order to support urban and agricultural prosperity and protecting the environment.
2: To set up the introduced system in the desired region.
I am so glad that anyone gives me useful advice and experience.
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Excellent and Impressive article best wishes
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In some areas where fresh water is scare, growers are desalinizing underground water to irrigate their crops. In one hand it looks good to overcome the shortage of water to continue growing the crops. On the other hand, beside the fresh water produced, the concentrated saline solution coming out of the reverse osmosis station is pumped back to the underground.
So, do not you think that this approach is more harmful to the environment and increases the salinity of the underground aquifer?
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Nice points of view. Thank you all for your valuable opinions. .
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We are launching a Ph.D. research looking at the effect of salinity and temperate increase on the bioerosion rates in coral reefs in the northern Persian Gulf. In doing so, artificial and natural blocks will be submerged over a gradient of salinity and temperature where hypersaline water from the desalination plant discharge into the sea. We are planning to use two types of natural and artificial blocks including (1) natural blocks by segmenting dead massive corals (e.g., Platygyra sp.); and (2) artificial blocks made of carbonate calcium.
But wonder how to make artificial blocks that need to be identical to natural blocks in terms of porosity and texture. Can we use crushed dead corals that have been blocked by a glue? If yes? What type of glue?
Wondering if anyone has experience in making such artificial blocks.
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You can use Lime Stone ( Calcium carbonate) blocks of any size needed & cemented - if at all - by Portland cement. These lime stone blocks are almost akin to natural corals in terms of porosity & texture. There are soft, medium & a bit harder varieties of Lime Stone. You can use preferably the first variety.
Dead corals are almost never porous - I mean the coral stones, which again can be cemented together by roughening the contact surfaces on both adhering surfaces.