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Bioleaching is another process that is being looked at for low-grade ores, ideal for reworking waste dumps.

This method, under atmospheric pressure, is being used in the Talvivaara project in Finland, a sulfide mineral resource of only 0.

Low-grade ores, like nickel sulfide, are abundant on Earth. Nickel sulfide deposits contain high levels of magnesium silicate gangue minerals MgO and can be difficult to process with conventional flotation and smelting technologies.

MgO is hydrophilic, which interferes with flotation of sulfide minerals, and reduces flotation recovery. In China, the Jinchuan Group Go.

Ltd has Mt of low-grade nickel sulfide mineral ores, and uses bioleaching for nickel recovery. This method is interesting, because traditional techniques using sulfuric acid are disfavoured, since magnesium silicate minerals are so reactive in acidic media - consuming large amounts of acid, which increases operational costs.

High-grade nickel ores are almost exhausted, since they are so heavily exploited and less abundant than the low-grade ores. High-grade nickel oxides are produced by fluid-bed roasting and chlorine-hydrogen reduction of nickel matte.

High-purity nickel pellets are produced by using vapour processes, an example of this is the carbonyl process: the copper and precious metals remain as a pyrophoric residue, which requires separate treatment.

Concentrating the nickel ores usually takes place close to the mine site, and involves chemical and physical processes to crush the ore and separate the nickel-bearing and gangue minerals.

Mining nickel directly is the obvious route to obtaining pure nickel, however, nickel can also be recovered as a byproduct of other metals.

For example, copper electrolysis requires a bleed to eliminate the buildup of impurities that accumulate over time as a result of the electrorefining of impure copper anode to produce pure metal cathode.

A bleed is required when certain impurity concentrations become too high in the electrolyte thereby adversely affecting the electrorefining performance.

The bleed stream is continuously withdrawn and replaced with fresh acid. This bleed stream is then further treated typically by neutralization to precipitate the contained metals.

Nickel can be recovered from the bleed stream of a copper electrorefinery. Classical methods for nickel recovery are precipitation, oxidation, and crystallization.

They are then separated from the mother liquor in a centrifuge, and dried and bagged for shipment. Soluble anode impurities continuously dissolve into the electrolyte, which is why they must be continuously removed from the bleed stream to prevent build up.

Another method for extraction of nickel from the bleed stream is the use of solvent extraction SX. Copper-selective solvents can be chosen, and many steps are followed to get nickel and copper powder from the bleed.

The following block flow diagram was shown in a paper by A. Agrawal et al. SX is a tool used in the processing of complex and secondary non-ferrous metal resources due to ease of metal separation, purification, enrichment, and analysis.

Similarly to the process shown above, certain solvents can be used to first extract copper, then adjust the pH to for extraction of nickel.

Copper SX plants are common, and they are a closed loop operation such that they use leaching and electrolysis to produce metal, while recycling the reagents in the system.

For example, SX can be used to extract and separate nickel and cobalt from chloride, ammoniacal, and sulfate solutions. Queensland Nickel uses a SX route where cobalt is removed as a sulfide by a reagent, then the loaded nickel is stripped with a high concentration of ammonia-ammonium carbonate solution, and the stripped solution is used to produce basic nickel carbonate.

Ammoniacal solutions are used in hydrometallurgical extraction of base metals because iron and manganese are rejected into the residue; solutions without these impurities can undergo metal separation by SX.

Some examples of ammoniacal solutions include ocean nodules, nickel laterites, sulfide concentrates, super-alloy scrap and other waste materials, and sulfate solutions.

Sulfuric acid is the most common medium for hydrometallurgical metal extraction; SX processes often report the separation of nickel and cobalt from dilute sulfuric acid solution.

This separation is carried out by cation-exchange type reagents. Ion exchange IX is used frequently in metal finishing industries for nickel recovery.

Some copper refinery tankhouses also use IX for acid recovery which involves treatment of the refinery bleed stream from liberator cells with short bed IX systems to produce a concentrated acid strip for recycle to the tankhouse , and an acid-free byproduct stream.

Another method of copper and nickel powder production, reported in by A. This method takes the copper bleed and uses hydrogen gas to produce copper powder.

The mother liquor with nickel sulfate solution then undergoes precipitation of copper with sodium sulfide to remove the remaining copper, followed by evaporation and crystallization to produce nickel sulfate crystals.

The nickel is releached with ammonia followed by hydrogen reduction to produce nickel powder, Figure 6.

Reduction of aqueous metal ions with hydrogen at high temperature and pressure can produce spherical particles, and hydrogen reduction of nickel can be done from different aqueous solutions.

Overall, I have only just scratched the surface when it comes to methods of nickel recovery. Since high-grade nickel ores are far and few between these days, fluid-bed roasting and chlorine-hydrogen reduction of nickel matte are becoming less popular techniques.

The recovery of nickel from low-grade ores is increasingly more important, from new techniques of pressure oxidation of the concentrate in an autoclave to bioleaching of the nickel in the ore, it is evident that time and money are being put into researching these processes.

Solvent extraction and ion exchange are also used in the recovery of nickel from various bleed streams from the electrorefining of other metals such as copper.

The unique properties of nickel such as corrosion resistance, conductive and magnetic properties, and the capability for electromagnetic shielding, are what make nickel such a valuable resource.

In the future, more recovery and recycling of nickel from secondary sources and low-grade ores will be even more important as ore grades decline and primary resources are depleted.

A grawal, A. Hydrogen reduction of bleed stream of an Indian copper industry to produce nickel powder. Materials Letters , 62 , pp.

Agrawal, A. Mineral Processing and Extractive Metallurgy Review , 33 5 , pp. Extractive separation of copper and nickel from copper bleed stream by solvent extraction route.

Minerals Engineering , 21 15 , pp. Anon, Mineral Commodity Summaries: Nickel. Ambatovy Overview. Ashcroft, G.

Cheremisinoff, N. Handbook of solid waste management and waste minimization technologies. Norwich, NY: Knovel. Cornwall, H.

Nickel Deposits of North America. Available from: ProQuest Ebook Central. Dalvi, A. The Past and the Future of Nickel Laterites.

PDA International Convention. Encyclopedia Britannica. Ikotun, B. Application of three xanthates collectors on the recovery of nickel and pentlandite in a low-grade nickel sulfide ore using optimum flotation parameters.

Particulate Science and Technology , 35 4 , pp. Jones, J. Can you see a major limitation of this method? How might this be overcome?

This is a rather involved problem, and must be taken one step at a time. The analyses of the cases for recycling each stream are similar, so the first case will be considered in detail and the second will be left for the reader.

Note: there is a mistake in the flow scheme. We have 4 unknowns and 2 equations at this point. This is where the problem solving requires some ingenuity.

First, lets see what happens when we combine this information with the splitting ratio and constant concentration at the splitter:.

Again we have more equations than unknowns but we know how to relate everything in these two equations to the inlet concentrations in the separator.

This is due to the conversions we are given:. Spend some time trying to figure out where these equations come from, it's all definition of mass fraction and translating words into algebraic equations.

Plugging in all of these into the existing balances, we finally obtain 2 equations in 2 unknowns:. Note: Notice that two things happened as expected: the concentration of the stream entering the evaporator went down because the feed is mixing with a more dilute recycle stream , and the total flowrate went up again due to contribution from the recycle stream.

This is always a good rough check to see if your answer makes sense, for example if the flowrate was lower than the feed rate you'd know something went wrong.

Once these values are known, you can choose to do a balance either on the separator or on the recombination point, since both now have 0 degrees of freedom.

We choose the separator because that leads directly to what we're looking for. The mass balances on the separator can be solved using the same method as that without a recycle system, the results are:.

Now since we know the flowrate of stream 3 and the splitting ratio we can find the rate of stream Note: You should check to make sure that m2 and m6 add up to the total feed rate, otherwise you made a mistake.

Now we can assess how effective the recycle is. The concentration of A in the liquid stream was reduced, by a small margin of 0.

However, this extra reduction came at a pair of costs: the flow rate of dilute stream was significantly reduced: from 45 to This limitation is important to keep in mind and also explains why we bother trying to make very efficient separation processes.

From Wikibooks, open books for an open world. Example : Suppose that in the previous example, a recycle system is set up in which half of stream 3 is siphoned off and recombined with the feed which is still the same composition as before.

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1 thoughts on “Bleed for this stream

  1. Guzahn says:

    Ich tue Abbitte, diese Variante kommt mir nicht heran. Wer noch, was vorsagen kann?

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