Sulfuric acid leaching of copper rich slag with the optimized parameters can provide a copper rich process solution with iron as the main impurity metal The solution can provide an attractive feed for integration into the industrial primary copper production with acceptable low Ni As and Pb levels g/L Cu g/L Fe g/L Ni g/L
Get Priceof sulphuric acid ii In the test where elemental sulphur was mixed with the copper ore the continuous generation of sulphuric acid took place which ensured the suitable pH and Eh for leaching most of the copper bearing mineral species due to the action of A thiooxidans in the operation conditions used iii The copper extraction results
Get PriceAll these compare favorably to the results of sulfuric acid leaching of chalcopyrite % recovery at 96 h Conichalcite proved less refractory to sulfuric acid 46 71% extraction in 10 g/L H2SO4 with 3 g/L Fe3 in 24 h and leached almost as well in MSA 45 67% extraction in 20 g/L MSA with 3 g/L Fe3 in 24 h but glycine thiourea and sulfurous acid did not effectively leach
Get PriceResearch is conducted on the factors affecting the copper leaching kinetic are temperature pressure concentration of sulfuric acid particle size The result shows that the apparent activity energy is KJ/mol We could determine that the copper leaching process is shrinking core model of chemical reaction control and work out the leaching
Get PriceThe effects of acid dosage baking temperature baking time and leaching time on the dissolution of copper and cobalt were investigated Sulphuric acid was added to the mixed copper cobalt oxide ore which was then baked in a muffle furnace To test the leachability of copper and cobalt from the baked material the reacted samples were exposed
Get PriceTherefore the sulfuric acid leach residue was % copper of which % was undissolved native copper The remaining copper may be assumed to be a sulfide copper with low solubility in sulfuric acid under the operational conditions The sulfuric acid leaching residue was neutralized with a sodium hydroxide solution and submitted to cyanidation At this latter stage 94% gold extraction was
Get PriceThe PEA states that the acid plant will produce million tons of excess sulfuric acid over the life of the mine Hudbay projects it will sell the sulfuric acid for an average of $145/ton Construction of an $88 million sulfide concentrate leach plant that will extract a copper laden solution from sulfide ore Hudbay says the sulfide
Get PriceStandardization of sulfuric acid Sep 25 2024 Explore Brooklynne Adamson s board Factorio Designs on Pinterest The ore sample contains 1 2 Ni 24 77 Fe and 0 062 Co The process applied includes digestion with 40 wt sulfuric acid at 200 C for 60 min roasting at 700 C for 15 min leaching with water for 30 min at 1 5 solid liquid ratio by weight and precipitation of the remaining iron at pH
Get PriceSulphuric acid heap leaching of nickel The method is an acid heap leaching method like that of the copper method in that it utilises sulphuric acid instead of cyanide solution to dissolve the target minerals from crushed ore The method has been developed by European Nickel PLC for the rock laterite deposits of Turkey and the Balkans See also Gold cyanidation Gold extraction Tailings
Get PriceNornickel Harjavalta are acknowledged for their support Our gratitude also goes to RawMatTERS Finland Infrastructure RAMI supported by the Academy of Finland Key words Cu cake autoclave leaching copper nickel converter matte sulfuric acid extraction hydrometallurgy precious metals Funding Information The work was supported by Act
Get PriceSulfuric Acid Sulfuric acid is a key element in the production of fertilizer phosphates and ammonium sulfate which is its primary use approximately 65% of total consumption Sulfuric acid is also used in the mining industry for leaching of copper nickel uranium and other elements from ores approximately 15% of total consumption
Get PriceThe sulfuric acid in a copper electrolyte is there for two reasons one is to keep the copper in solution you only used a 0 1 m solution if you use higher concentrations your copper sulfate will partially get Cu OH 2 Also the sulfuric acid gives you a better conductivity and with this comes a better throwing power Throwing power is the ability of the electrolyte to get uniform depositions
Get PriceThe leaching of Cu metal was enhanced by adding Cu 2 ions and introducing O 2 in the sulfuric acid solution the leaching efficiency of Cu increased to more than % within 30 min in 1 mol/L sulfuric acid solution with 10 000 mg/L Cu 2 at 400 rpm with 1% pulp density <75 µm particle size and 100 cc/min O 2
Get PriceQuestion Video Reaction of Sulfuric Acid with Cupric Oxide Ores containing cupric oxide CuO are commonly reacted with sulfuric acid to produce a copper containing material that is more easily processed This process is known as sulfuric acid leaching a Write a balanced chemical equation for the reaction of cupric oxide with sulfuric acid
Get PriceThe copper ore contains the sulfur you use to produce the sulfuric acid which in turn you use to leach out the other impurities in the minerals Extracting hydrogen from sulfuric acid with solar uses much less energy than water electrolysis Using sulfuric acid both hydrogen and oxygen can be generated in a new kind of solar reactor In the
Get PriceThe reaction between copper carbonate and sulphuric acid will be a neutralization reaction Copper carbonate will acts as a base however sulphuric acid is an acid This reaction can also be viewed as a double displacement reaction too Let s understand the nature of this reaction and what will be the final product of this reaction
Get PriceLeaching behaviors of zinc copper indium and iron from a sphalerite concentrate in sulfuric acid oxygen system has been investigated in the present paper Various parameters were studied including particle size concentration of sulfuric acid partial pressure of oxygen leaching temperature and leaching time The experimental data indicated that under the typical plant conditions employed
Get PriceThe study investigates the effect of particle size temperature acid concentration agitation and leaching time under oxidizing conditions The results showed that at optimized conditions 40 °C 2 M H2SO4 60 min leaching time kW/m3 mixing power and 2024 mL/min oxygen flow rate ca 100% extraction of copper from slag into the
Get Pricemum copper recovery in sulphuric acid and hydrochloric acid leaching experiments at normal pressure was found to be about 55% and 77% respectively In both the cases nickel and tellurium recoveries were poor In the autoclave leaching copper and tellurium recoveries improved with increasing time and pressure Maximum copper and tellurium recoveries to the tune of 85% and 71% respectively were
Get PriceCopper tailing is a widespread and intractable solid waste in copper production Traditional leaching and recovery technology for copper tailing focuses on copper but neglects the leaching of iron With the increase in applications and demands of iron containing materials for environment understand …
Get PriceHigh concentrations of sulfuric acid 85 90% are used to increase the e ciency of leaching processes At the same time the temperature in the reaction mixture rises to a temperature range of 200 220 C due to the exothermic reactions of the leaching process and the interaction of concentrated acid with sharp water steam
Get PriceFeb 2 2021Copper tailing is a widespread and intractable solid waste in copper production Traditional leaching and recovery technology for copper tailing focuses on copper but neglects the leaching of iron With the increase in applications and demands of iron containing materials for environment understand …
Get PriceThe production of fertilizers especially phosphate fertilizers from wet process phosphoric acid is the major end use market for sulfuric acid accounting for over 60% of total world consumption in 2024 This share is expected to slightly decrease through 2024 mainly because metal leaching and steel pickling applications are expected to grow at a higher rate About 14% of global sulfuric
Get PriceDOI / Corpus ID 159398659 Sulfuric acid leaching for capturing value from copper rich converter slag article{Khalid2019SulfuricAL title={Sulfuric acid leaching for capturing value from copper rich converter slag} author={Muhammad Kamran Khalid and Joseph Hamuyuni and Vivek Agarwal and Jouni Pihlasalo and Mika Haapalainen and Mari Lundstr{ o}m} journal
Get PriceSulfuric acid injection in copper heap leaching LEWA LEWA process pumps are used to reinject sulfuric acid at 98% into the main pipelines that go to the heap leach sprinklers Tel 49 7152 14 0Contact LEWAGroup Downloads Representatives Finder Contact Career contact phoneexplore Pumps Pumps Metering Pumps Process Pumps
Get PriceMay 16 2022The leaching solution was made using distilled water and sulfuric acid H 2 SO 4 The lixiviant was prepared in different concentrations according to the working conditions The temperature was controlled by a probe permanently placed in the leaching reactor and regulated using a thermostat
Get Priceand mechanism of the leaching of iron from copper tailings using sulfuric acid were studied Under optimal conditions 40 C sulfuric acid concentration of mol L1 stirring speed of 400 rpm solid/liquid ratio of 1 10 and leaching time of 120 min % of Fe along with % of Zn and % of Cu were leached from the tailings
Get Price2024 Yoo et al Metals A new concept for copper Cu metal leaching by the simultaneous use of cupric ions Cu2 and oxygen O2 was proposed to improve Cu metal leaching in sulfuric acid According to this concept Cu2 oxidizes Cu metal into cuprous ion Cu and O2 oxidizes Cu into Cu2
Get PriceEnvironmental Impact of Sulfuric Acid Leaching The electro winning system [SX EW] of extracting copper is a step in the right direction as the mining industry attempts to develop methods that have less of an impact on the environment Really it s a huge step since it eliminates tailings impoundments which are unsightly and can cause water
Get Priceleaching in 1 and 2 1 sulfuric acid solutions The subsequent leaching was performed in the optimized acid concentrations at temperatures of 25 45 65 and 85 °C for 1 and 2 hour at each temperature A variable speed stirrer operated at a speed of 100rpm was maintained during in all leaching experiments at
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