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In your opinion, which programming language would you suggest as the best choice for researchers specializing in hydrology and water resources?
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Python Is the most versatile language, widely used in hydrology and water sciences, and has excellent libraries for data analysis and AI-related tasks ¹. Its ease of use and flexibility make it perfect for researchers.
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Dear colleagues,
I would like to inquire about the latest advancements in technology for monitoring hyporheic flow. I am interested in any methods, whether data-driven, numerical, or analytical, that can be used to directly or indirectly monitor and assess hyporheic flow.
Thank you 🥹🥹
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The theoretical prediction that the concentration in storage is much greater than the tail of the in-stream breakthrough curve supports recommendations that in-stream measurements should be supplemented with direct measures in the hyporheic zone , In fact, sensitivity limits on in-stream measurements can often make it impossible to distinguish hyporheic exchange from in-stream data, making it essential to obtain direct subsurface measurements.but this can be substantially improved with basic field measurements of stream velocity, average depth and streambed slope, dimensions of major classes of topographic features, and bed hydraulic conductivity, followed by use of published statistical relationships or simple scaling laws .There is considerable interest in using heat as a tracer of hyporheic exchange because fluid temperatures can be measured quickly, easily, and reliably, and natural temperature fluctuations provide a signal in surface water relative to groundwater.
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I am currently synthesizing membranes for drinking water treatment and would like to use non-toxic solvents such as or better than Ethyl lactate. If you have done any research in this field or you know of any compound that I can use, kindly provide me with that information. 
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I am looking for collaborations in environmental sciences. Especially in Water technologies (Water quality, Water treatment, Water management....)
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Dear Akuemaho Akowanou , I complete My B.Sc (honours) degree in Environmental Science and Disaster Management from Bangabandhu Sheikh Mujibur Rahman Science & Technology University, Gopalganj, Bangladesh. I am highly interested to join your labratory.
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For example: Iran falls within the Middle East arid zone, with some 13% of the country receiving less than 100 mm mean annual rainfall, an additional 61% receiving less than 250 mm and only 9% receiving more than 500 mm.
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Do I use direct solar radiation during a day or global solar radiation during a day.
help me please 
thanks advance 
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Solar still efficiency = distillate × hfg/ Total solar intensity × glass area× time
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As per the latest research, Microsoft finds underwater data centers are reliable, practical and use energy sustainably so how can we enable IoT with LoRa technology in the underwater data center for making those data center more efficient ?
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It would enormous task. But currently, research directions are moving towards such applications.........I think humans will not leave any natural resources.....:)
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Plotting specific conductance versus total dissolved solids (TDS) from measured water quality data from water wells in the Hill Country region of Texas, United States, yields two distinct trends (Figure 1). This presents a problem when estimating TDS in this region, either from measuring specific conductance from water samples, or from calculating formation water resistivity from geophysical well logs. The two trends were visually isolated (Figures 2 and 3) for comparison of chemical, spatial, and formational patterns between the two. Analysis of the two trends reveals the water for each is identical in terms of major and common minor constituents (Figure 4), the two trends occur in all formations of the Trinity aquifer system, and there is no overall regional pattern of one trend vs the other, though the trends locally cluster (Figure 5, example from the Upper Glen Rose Formation). Water of both trends are dominated by Ca-Mg-HCO3 and Ca-Mg-SO4, and as TDS increases, calcium-magnesium-sulfate becomes the dominant water type, with up to 94% of the total milliequivalents per liter comprised of Ca-Mg-SO4.
Initial thoughts were the difference in the trends could be explained by ion complexing in some areas but not others, perhaps catalyzed by subtle geochemical constituents in the subsurface, or Eh-pH conditions (there is no significant difference in pH between the two trends). But current thoughts are that ion complexing cannot explain a nearly 50% reduction in specific conductivity from the lower trend to the upper trend (given the same TDS value), which would require nearly 50% of the ions to form complexes. Other hypothesis is the difference between the two trends could be due to bias in sampling and analysis. Perhaps for the upper trend nearly 50% of the Ca-Mg-SO4 precipitates as solid CaSO4 and MgSO4 when sampled and specific conductance is measured (measuring a low specific conductance relative to the weight of constituents in the water), whereas the sample is then mixed at the laboratory and the precipitate is re-dissolved before analyzing the concentration of constituents. This is only a conjecture. I am not a geochemist and I have rudimentary knowledge of water sampling procedures – my background is primarily geologic mapping and structural geology.
Points of discussion regarding this are:
· What are the potential explanations for two significantly different trends of TDS versus specific conductance for otherwise identical water types? Keep in mind the water types in this case are dominantly Ca-Mg-HCO3 and Ca-Mg-SO4 (the latter dominating at higher TDS)
· Could ion complexing be responsible, or is the magnitude of decreased specific conductance demonstrated above too great?
· Do you know of any other studies where two trends of TDS versus specific conductance has been examined for a region, or other relevant publications?
· Which of the two trends are more likely to occur in the subsurface? Or is it likely they both occur locally in the subsurface? (Our goal is to estimate TDS from resistivity logs; thus, we need a single, reliable TDS vs specific conductance trend)
· Are you familiar with collecting, sampling, and analyzing water samples, and have some insight into whether the specific conductance could measure relatively very low for a given quality or water?
A copy of the data is attached (there are two tabs, one for each trend). Thank you for considering this problem!
Evan Strickland, P.G. | Geoscientist
Texas Water Development Board
Innovative Water Technologies | BRACS team
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Credit is due to F. Paul Bertetti, P.G., who identified this lab as a source of erroneous conductance measurements in an unpublished report.
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If i am using the demineralized water with the PH of the 5 to 6 & conductivity of 100-150 μs/cm to clean the aluminum alloy, can it cause a corrosion to aluminum?
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pH of DM water on aluminum finishing lines is usually in range of 5.5-5.7. The water with this pH can't cause corrosion. Most of aluminum alloys, except 7XXX and 2XXX can stay in DM water with this pH range for long time. It is a normal case on big multi-processes aluminum finishing lines to use the bathes with DM water as a buffer. However, it is important to control chlorine concentration in the bath. It should not exceed 100 ppm.
On other side, conductivity of your water is relative high for DM water. Usually, it should not be higher than 100 μs/cm for general industry and 50 for aerospace finishing. DM water with electrical conductivity 100-150 μs/cm might attack 7XXX alloys, for example 7075 or 7175.
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Hi, I currently work for Innoscripta, a company based in Germany. We are constantly searching for innovation projects to build up a research grant. Our role is to tie up this innovative projects with small and medium-sized companies (SMEs) who can adapt these innovation ideas.
We are looking for English-speaking junior professors in need of getting a full professorship or doctoral researchers in Germany in need of constant funding. We are looking for innovative ideas under the following sectors: sensors, machine building, automation, robotics, food & beverage, construction (e.g. new type of concrete), water technology, renewable energy ideas, everything which can turn into a quick profit, software topics together with hardware (digitalization is a huge topic in Germany).
I am particularly looking to tap these individuals so it will be helpful to have a link on groups/ discussions/ pages on where I can join and send my proposals for collaboration with them. Looking forward to all your help!
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would someone please explain to me what is PAC learning and empirical risk minimization?
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I would like to ask and discuss.
Have anyone done research on the biogas production with additional of treatment using subcritical water technology? I have difficulties and confusion, as when I did preliminary experiments towards the treated and untreated material, according to hyphothesis should be the treated material produced the highest biogas production. However, the actual results were the opposite.
Did anyone encounter this type of findings?
Thank you.
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Hi @Nadia
It is true what Dr. @Bachmann mentioned that it is better to do carbon balance. Some parts of the substrate carbon may have been decomposed to gaseous or volatile compounds during heating.
In addition, the heating process may produce compounds that are toxic to microbial communities involved in AD process. So, it may be better if you do analysis about these toxins as well in the substrate.
Regards,
Alam
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I have treated my highly contaminated water to make it soft but although i managed to make it soft water, the TDS is still the same as i used Cations Exchange Method.
So, Is there any method to reduce the TDS of the contaminated water?
Suggestions would be highly appreciable!
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Reverse Osmosis, and Ion Exchange Treatment.
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I read in a paper that says: Dating ancient water technologies often difficult and published ages are often imprecise.
Why it is difficult to date?
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No is not difficult
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Hello everybody, I have been overwhelmed by the responses I have had to the Process Stress in Wastewater Treatment Survey. This is the last time I will be posting the survey before it closes. So please, if you can spare 10 min to fill in the survey it would be greatly appreciated. Thank you again for your support!
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Through the Advanced Oxidation Processing
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The idea is to remove organics from seawater to reduce fouling problems or remove organics from treated wastewater to improve reuse applications.
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For Pre and post both,for recycling purposes we have to adopt the new technology (Nano technology) for treated waste water to recycle the treated waste water ,Major problem of recycling is COD and BOD.
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I must compare solar still with different material that finds the cheapest option to propose in an industry case of curse my be have to use the expensive material . one of the important section is the choice of top cover it must be transparent, resistant and cheap as possible as .plexi glass and polycarbonate are proper but its expensive. please guide me to choice proper cover. 
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Clear Acrylic sheet 
Regards 
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Looking for any recent research or innovations on the water treatment. Work with poor communities in rural Africa and most current treatment systems are very expensive for the community. Would there be any appropriate technology solutions? Recently drilled two boreholes near Lake Turkana with good yield but water is too salty for drinking and farming as well. Also ideas of how to use this water would be welcomed.
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Waste heat source includes industrial/ institutional/commercial waste heat. How much heat (in kW) that you get as an average throughout the day.  What is quantity of water input that you feed for desalinatio
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There is no waste heat in solar distillation, if heal loss is done, the efficiency will drop
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i am making a prototype for RO desalination system and want to know the least pressure for effective freshh water production, and at that pressure what is the flow rate per unit area of the membrane?
and if you can give further articles or papers.
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You must know the feed seawater condition and the feed after chemical pretreatment from SDI, pH, TDS, and the temperature. Then you can choose the appropriate type of membranes. The least pressure, is the pressure just greater than the net driving pressure (which  depends on the feed TDS).   
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The main drawback of the Forward osmosis (FO) desalination system is the lack of efficient draw solution recovery process.
How does the recovery unit take out the draw solution from the potable water?
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Dear Nabil,
In my understanding, the methods used to separate the draw solute from water after FO depend on the properties of the draw solutes. For the commonly used inorganic salts, such as NaCl, RO is used. For the synthetic draw solutes which are the research focus in recent years, the posttreatment approaches are diverse. For example, magnetic nanoparticles which have been used as draw solutes can be separated from water via a external magnetic field. The following links are for your reference
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Our lab has Perkin Elmer LS 55. I am going to use it for characterizing DOM in surface water. My questions are:
1. Does this instrument can record data in ratio mode accounting for differences in lamp intensity at different excitation wavelengths?
2. How to know the spectral correction factors from the instrument?
Thanks for sharing your opinion.
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Dear Euis 
Yes you can use the perkin Elmer at different excitation wavelengths. you can scan your sample at different excitation wavelengths to build the 3D spectrum. Actually I am using the same equipment and you can to make the correction of spectrum using water.
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Produced water is the water in the same formations of oil and gas, that has been brought up to the surface with the hydrocarbons. I try to find a standard method for making synthetic produced water that could imitate similarly to that offshore. I was wondering if there is any specification on synthetic produced water and does its characteristic differs for every region? 
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to get a copy of 
ASTM D1141 - 98(2013) - Standard Practice for the Preparation of Substitute Ocean Water, the link:
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The automated drinking water treatment plants use an automatic coagulation control system to define the required chemical dose without manual intervention (Jar testing).
However, the control system might be based on different models. The dose might be defined as per the raw water quality, the surface charge of the floc or the treated water quality.
Could you please advise what is the common engineering practice for the chemical control doses and what is the recommended model for high raw water algae loads.
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Dear Hassan,
The attached recent review article entitled " State of the Art of Online Monitoring and Control of the Coagulation Process " by Harsha Ratnaweera  and Joachim Fettig published in Water 2015, 7, 6574-6597; doi:10.3390/w7116574 describes the commonly used feedback systems  for automatic coagulation Control in water treatment:
Abstract: Coagulation is an essential process for the removal of suspended and colloidal material from water and wastewater. However, no comprehensive or universally accepted mathematical description of the process has been developed so far. Therefore, process optimization and control is usually based on data from jar tests and simple flow-proportional dosing concepts, while more accurate concepts based on water quality parameters that can be measured online are emerging. In addition, there have been attempts to develop software sensors and control schemes that involve advanced mathematical analyses of these parameters. The paper presents an overview of the parameters and physical sensors that are
used for feed-forward and feed-backward control schemes and the experiences that have been made with their implementation. Moreover, the development and use of software sensors is described. Finally, the practical applications of different control techniques are given in order to illustrate the state of the art of coagulation control. Some thoughts about research needs conclude this review.
Hoping this will be helpful,
Rafik
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Equations
Previous studies
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Siltation will increase the evocation by two ways  by reducing the storage capacity  ( increasing the surface area and by absorbing higher solar  radiation
The first effect will be significant  only for heavy siltation the second  if the turbidity is high 
You can study both effects by lab experiment by assessing the  S'S and turbidity   levels and  corelating  to lake or pond topography. 
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Am interested in optimizing neutralization during water treatment when using polyaluminum chloride. I need to understand the charge density of the raw water so that I can make the right specification of a polyaluminum chloride with a higher charge density. The challenge I have is how to determine charge densities of the raw water and that of the polyaluminum chloride. Is there someone who has experience in these issues?
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Dear Rafik,
The first link could not open. The pdf you attached is for methods polyelectrolytes, Am more interested in inorganic polyaluminium chlorides. Do you have the procedures for titration method?
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I am going to plan a work on salinity screening in pot, Can i use a sea water for treatments?
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Thanks sir
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What are the materials used, its processes, and the demand of the methods in present time? It would be really helpful if you would include a link or a website as reference. Thank you! :)
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Dear Rodgin Grace,
In my knowledge, there are 2 usual methods of water softening. First, precipitation method which use chemical (lime and soda) in its process. The process is just adding and mixing chemical to hard water and the sludge will be precipitated. Second, ion exchange method which use resin in its process. The process is pumping hard water to the resin column, then Ca(II) and Mg(II) ion will be exchanged by Na(I) ion.
There are also some new methods of water softening like membrane process, distillation, and magnetic water treatment. The most developed new method is membrane process.
For the detailed process, you can read in Unit Operations of Environmetal Engineering by Reynolds. You can find this ebook in scribd application for android. For membrane process in water softening, you can refer to the link.
I hope my explanation can help you.
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Dear Colleagues
In case that the salinity of oilfield or brackish water is high, a possible method is blending the treated flow with high saline feed water (to dilute the input salinity). Is there any other more intelligent process available? - Any data or experience about / with High Efficiency Reverse Osmosis (HERO)?
Thank you in advance!
Ruediger
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One possible alternative is Forward Osmosis..
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Can anyone suggest some media filter for building greywater treatment and is there some new technology for it?
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Hey you can use Bark and Charcoal as a filter media? Bark filter will help to remove high BOD load
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Test Method 1311: Toxicity Characteristic Leaching Procedure (TCLP) in “Test Methods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA Publication SW–846 and EPA, 40 CFR, Part 261 is widely used, not only in the US.
The associated parameter list is the so-called D-list aka D-codes which includes 43 single parameters but next to many others, what you commonly can re-calculate from the US Drinking Water Ordinance "CYANIDES" are missing.
Any idea, why such a vital parameter was not listed?
Thank you and Glück Auf!
Dr. Rüdiger B. Richter
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Weak acid dissociable cyanide criteria limits are available in some regulations and standards as available in the Guidance Document, Department of Environment Pollution Prevention Division, Guidance Document, GOVERNMENT OF NEWFOUNDLAND AND LABRADOR.
But for total cyanide, may be criteria limits are not readily available. Additional research may be required.
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There is question in chapter 7 of book" Wastewater Engineering, 2014"
In Eq 7-61 it is mentioned that COD equivalent of cell debris is considered in "Px,bio". But in Eq. 7-25 only net rate of biomass growth ("rx") is considered in the equation. It is logical that the Eq 7-25 be modified to (rsu -1.42(rx+rx,i)) in which the rate of cell debris is regarded. What is your opinion?
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It is the same problem in edition 2003 as in Eq. 7-24 and 7-59 respectively. I think the second equation sounds more logical which tells that a fraction of bCOD is converted to a nbCOD as cell debris (endogenous residual). So in my opinion Eq 7-25 in 5th edition (2014) or Eq 7-24 in 4th ed. (2003) should be modified.
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I have to be sure, If we have a wastewater with zero BOD,can we treat that with biological ways? using microorganisms? 
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I think you should provide more information about the wastewater. If your WW has COD that is not biodegradable then you may think to have a pretreatment step (e.g. ozonation, AOP) before the biologiocal step. Having only nutrients (PO4, NO3 etc.) in the WW without a source of carbon is not enough for biodegradation and after all what are you going to biodegrade.
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I am using a strainer to pre-treat Lake water for a UF membrane system. We performed Particle size distribution analysis on the Feed, Filtrate, Backwash water. Our data showed that the number of particle count after the strainer is higher than the feed (before strainer).
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Yes it can be normally observed in ultra-filtration. Because UF performs under the pressure. At high pressures the particles which have coagulation's tend to break up.
By DLS analysis of filtrate and feed, the changes can easily identify. 
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Dear Colleagues, 
I am looking for papers (only web-links) explaining how to prepare an aqueous solution of fully dispersed powdered activated carbon (PAC), even if fictionalization of PAC is required. 
Regards,
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Paper #90 presented at the Power Plant Pollutant Control Mega Symposium (April 19-22, 2014) by Ariel Li of ADA Carbon Solutions presents a carbon that is able to be water dispersed. The paper is titled "Field Demonstration of Advanced Activated Carbon for Mercury Control in Wet FGD".
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This could be either an elevated or a ground level water storage tank . Thanks very much!
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Hello. Thank you very much for the help. I have been able to source the necessary information :) 
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Most atmospheric water-vapour harvesting methods, which I found so far, are based on the principle of dew formation. Triggering adsorption by moving air passed an hydrophobic / hydrophilic object (e.g. foil) which is cooled below dew point.
Are there any projects known/research done where a desiccant-fibre (e.g. Wool, Cotton, Polymers) absorbs atmospheric water-vapour in hydroxyl groups and/or amorphous areas when being exposed to air?
The harvesting happens in a second step when increased energy ‘breaks’ the water away from the desiccant. So far, I know only of one company (www.aquasciences.com) which is using this principle, charging a salt.
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i had an experience . when i  put a few onion and garlic on the sand or LECA in the pot which there was a little water in the bottom of it , the tubers grew very well whiout any access irrigation
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Manufactured caustic usually contains chloride ranging as high as hundreds of ppm chloride. There is an existing process for reducing chloride to less than 10 ppm. We are considering developing  a new process to reduce chloride to less than 1 ppm. Which processes can you identify that need less than 1 ppm chloride?
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Yes it would be of interest for applications such as for Semi Conductors and Electronics where contamination levels may be as low as PPT levels. 
Low chloride caustic soda would also be of interest for boiler pH control applications. 
It may also be of interest for the rare earths industry 
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As we know, to prevent air pollution (like Total Suspended Particulate) on a construction site or concrete mixing batching plant, we usually use water and no further water treatment from used water (especially in my country). I want to know what is contained in that water and what method I should use to determine water quality.
So, if your country has better technology to prevent air pollution than use water and technology to treat used water from construction site, kindly tell me.
Thank you.
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Thank you Geoffrey Marchal, Mohammed j.k Bashir, Taratisio Ndwiga
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Present SVI= 120 ml/gm; required SVI= 80 ml/gm
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There are several reasons for high or low SVI, few details can give idea about the exact cause like, effluent type, design operations, MLSS/MLVSS, DO, pH &Temperature. Which can further troubleshoot by several ways. However, more than 1.5ppm DO surely would be helping to improve settling but it’s depend on design parameter/availability of aerators/diffuser or energy costing. I agree with chlorination or adding peroxide in RAS/clarifier, but if DO is already good than cause would be different.
While as per my real experiences by doing some operational changes and external EPS producing bacterial seeding surely would be improving SVI/ sludge settling. Recently troubleshooting of 15 MLD activated sludge plant (Textile) we face high SVI and TSS carry over problem and analysis showed very less bacterial population/high TDS/very low performance, while DO was almost near to 2ppm. I started external multiplication of EPS producing bacteria (from sludge only) and controlled recycling rate along with systematic draining of old sludge. After 10 days SVI improved almost double and found improved performances by 40% higher.
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What are the test methods for determining Residual Chlorine and Residual Ozone in water ?
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The different scopes of upgradation for an SSF / RSF based water treatment plants needs to be explored to ensure supply of safe drinking water. Upgradation of a water treatment plant might be necessary due to many reasons as follows:
(i) Expiry of the design period.
(ii) Increase of coverage area resulting in increase in demand.
(iii) Population increase
(iv) Changes in raw water qualities
(v) Changes in scopes / natures of treatment etc.
So what are the practical scopes for this purpose? What are the scopes of dual media filtration in this regard?
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Respected Atul Mittal Sir,
I am very much delighted to get your kind updates to my question. Sir can you remember me that I am one of your students (in the M. Tech batch 1999-2000)?
By the way, I would like to request for your kind guidance (in future) for different issues related to the upgradation of existing drinking water treatment plant.
Thanking you.
Best Regards.
Nripendra Kumar Sarma
Nagaon, Assam, India
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Nutrient removal
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HRT is not a critical design and control parameter to consider but solids retention time (SRT). This is depending upon the wastewater temperature. For example a total SRT of 10-12 days would be sufficient at wastewater design temperature of 20oC whereas total SRT of more than 20-25 days is needed at 10oC. Anoxic and aerobic SRTs are depending on feed wastewater quality, target effluent nitrogen configuration and process configuration. IWA based simulation models (i.e., Biowin, GPSX) are available to determine anoxic and aerobic SRTs.
Design engineers provide adeqaute tank volume to keep the biomass in suspension and allow proper mixing and oxygenation all of which dictate the minimum HRT. Although HRTs may vary, typical minumum anoxic and aerobic HRTs in MLE systems are 1.5-3 and 6-10 hrs.
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I measured the protein (PN), polysaccharide (PS) of surface water for drinking water analysis. But as we all know, the concentration of PN & PS are too low to be detected. Therefore, I want to use lyophilization to concentrate the water samples. However, I can not find any papers talking about using this concentrating method. I am just wondering if anyone has any experience with lyophilization or water sample concentrating. Is lyophilization a feasible method to concentrate water samples.
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I think a partial lyophilization will be suitable. However I think that you can get similar results with vacuum evaporation which is easier and less time consuming.
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I need a smaller flow rate less than 10 ml per minute.
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If you are unable to use a pump with smaller nominal flow rate, or you have not the possibilities of reduce the speed of rotation, I think you will applicable only a "creative ways"...
One such the "creative ways" is to dividing the flow of liquid downstream of the pump into two parts. Next - experimentally - can adjust the flow rate of the two streams, so, that one of them will be identical to what you need, and the other - redundant - can be returned to the original container of the liquid.
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We collected the waste water sample from a sewage channel. The BOD/COD ratio of the sample is in the range of 0.009 to 0.02. What may be the reason for a very low BOD/COD ratio? How can we connect this BOD/COD ratio with biodegradability?
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There can be different reasons for this. The simplest one is that the BOD test is wrong. Also the COD test may be wrong (overestimation of COD due to interferences). Another possibility is that there are some inorganic and/or organic pollutants in the sewage sample (probably due to heavy industrial inputs) that inhibit the bacteria in the BOD test and thus lead to a wrong BOD reading. Another possibility is that the biodegradable part has been rapidly depleted in the sewer due to extreme temperatures etc. But , I think that this is unlikely to occur.
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Sodium borohydride is a versatile reducing agent. Is it safe to use in water treatment processes, considering the possible byproducts such as boric acid, Hydrogen gas etc.,