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residence time in leaching tanks

Leach circuit residence time testing HydrometallurgyThe efficiency of the leaching process greatly depends on the flow structure created by mechanical agitation (in some cases air agitation) in the leaching tanks. Residence time distribution (RTD) measurement was conducted in the CIL section of a gold processing plant in order to determine the flow structure in the first tank using the 131 I radioactive tracer. The shape of the experimentalEstimated Reading Time 8 minsResidence time distribution of an industrial mechanicallyMay 01, 2005· The ideal continuous stirred tank reactor (CSTR) (9) G c (s) = 1 τ s + 1 where τ is the average residence time of the liquid, gas or solid inside the reactor. (b) The ideal plug flow reactor (PFR) (10)

Residence time distribution of an industrial mechanically

May 01, 2005· The ideal continuous stirred tank reactor (CSTR) (9) G c (s) = 1 τ s + 1 where τ is the average residence time of the liquid, gas or solid inside the reactor. (b) The ideal plug flow reactor (PFR) (10) G p ( s ) = e τ s where τ is the delay or the residence

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MODELING OF THE CARBON IN PULP (CIP) PROCESS IN GOLD

cyanide solution to obtain slurry above pH 10 and by supplying oxygen to leach tanks. Dissolution of gcyanide completes in about 24 hours. The hydrometallurgical reaction for extracting g from its ores can be expressed as below the residence time of the carbon for each tank, the stripping amounts per week, the adsorption tank amount

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v116n6a5 Optimization of circuits for pressure leaching of

The performance of leaching reactors depends on three factors residence time, leaching kinetics, and particle size distribution. These factors are combined in the leaching number, defined by Crundwell (2005), according to Equation [10] [10] where r s is the rate of shrinkage of particles, t is the mean residence time, and l is the

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v118n5a2 Test work to examine the potential for improving

carboninpulp leaching, and electrowinning. Figure 1 shows the layout of the leach section, which consists of one preoxidation tank and eight leach tanks with a total residence time of approximately 18 hours. The throughput is 200 t/h with the feed at 75% passing 75 μm and pulp density 50% solids. Oxygen is injected into the tanks to

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Leach Circuit Design Principles SRK Consulting

Designing a leach circuit should consider both orespecific factors as well as factors involving the interaction between the ore and process equipment. Achieving the optimum leach performance involves combining operating parameters, such as grind size, residence time, chemical conditions (reagent addition levels, temperature, etc.), most of

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Determination of Flow Structure in a G Leaching Tank by

Residence Time Distribution, Computational Fluid Dynamics, Navier Stokes Equations, EulerianEulerian MultiFluid Model, RANS Standard kε Mixture Model, Multiple Reference Frame 1. Introduction G leaching tanks are typical continuously stirred tank reactors (STRs) that are used in the n metallurgical i *Corresponding author.

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Tank leaching BioMineWiki

Feed slurry, finemilled to a grind size of d90 = 12 μm, was added to the reactor at a residence time of 3 days. Advantages . Tank leaching allows for good process control and contact between leaching reagent and material to be leached which therefore results in faster leaching kinetics and better recoveries. rapid recovery of the desired metal

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Measuring pH in Cyanide Leaching

The leaching process is conducted in leach tanks that have a total residence time of about 24 hours. The g cyanide in the pregnant solution is adsorbed on granular activated carbon inside the carbon in pulp (CIP) tanks. The coarse laden carbon

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(PDF) RESIDENCE TIME DISTRIBUTION (RTD) IN OPERATING PLANT

The efficiency of the leaching process greatly depends on the flow structure created by mechanical agitation (in some cases air agitation) in the leaching tanks. Residence time distribution (RTD

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CIL G Mining Solution Mineral Processing

Sufficient residence time is provided in each tank to facilitate the leaching. Carbon particles are suspended in the tanks to simultaneously adsorb g from cyanide solution. Screens are installed in each tank to prevent carbon transfer along with the ore.

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Radiotracer investigation in g leaching tanks

Abstract. Measurement and analysis of residence time distribution (RTD) is a classical method to investigate performance of chemical reactors. In the present investigation, the radioactive tracer technique was used to measure the RTD of aqueous phase in a series of g leaching tanks at the Damang g processing plant in Ghana. The objective of the investigation was to measure the

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what are the effects of leaching time on g recovery

Residence time in the CIL circuit is the time taken for the slurry to flow through the tanks, and is an important operational consideration. The longer the g particles are in contact with the cyanide in the slurry the more g that will be leached.

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Leach circuit residence time testing Hydrometallurgy

The efficiency of the leaching process greatly depends on the flow structure created by mechanical agitation (in some cases air agitation) in the leaching tanks. Residence time distribution (RTD) measurement was conducted in the CIL section of a g processing plant in order to determine the flow structure in the first tank using the 131 I radioactive tracer. The shape of the experimental

Estimated Reading Time 8 mins Chat
Residence time calculation Chemical process engineering

Sep 21, 2006· The residence time of the liquid is the ratio of occupied vessel volume, at the required level, divided by the liquid flow rate. Liquid hup depends on the service, for example, whether it is to be used as a reflux drum, or if it is intended to allow separation of water from hydrocarbons, etc. b. For efficient V/L separation, it is the

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(PDF) G Loses due to Silt Formation in Leaching Tanks

The results presented in this study demonstrate that the residence time of these particles in the grinding circuit can be as long as in the leaching tanks and might be the dominant factor in

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Residence time distribution of an industrial mechanically

Note that in the present case the average residence time in the first leaching tank was estimated as about 60.8 min (de Andrade Lima and Hodouin, 2005b), which is the same order as the estimated

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Control of pH in the cyanide leaching process June

Plants now also commonly inject oxygen into the leach tanks to help accelerate the leaching process. Since oxygen is a key component in the above reaction, it increases g recovery for a given residence time in the leach tanks. Usually the leach tanks are large and contain only cyanide solution and pulp.

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The process design of g leaching and carboninpulp

Although air agitated leach tanks were commonly used in the industry, mechanically agitated reactors are preferred due to lower operating costs. Typical residence times in the leach section may range from 2040 hours depending on the headgrade and nature of the ore and the number of leach reactors in series may range from 6 to 12.

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Grinding down costs CIM

Mar 21, · The reasoning behind this was that early cyanidation could limit the residence time required in leach tanks further down the line, keeping the circuit size small. But COREMs work found that much of the cyanide injected at the grinding stage was being consumed in reactions with steel grinding media and other minerals in the ore.

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APPLICATION OF LEACHING KINETICS MODELLING TO A

per hour), solid concentration (%) and tank volumes (m3), residence time (h) and flow rate (m3/h), of the slurry in each tank were calculated. The plant data for the five seperated sampling conditions were shown in Tables 1 and 2. Table 1. Plant data for the five different samplings Leaching time (slurry residence time in tank) t, hours

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The Direct Nickel Process Total Materia Article

The residence time in the leaching tanks is between 26 hours with 4 hours being typical. During the leaching around half of the mass of the ore is dissolved into the nitric acid, leaving behind the acid insoluble minerals, usually consisting of silicates, and the pregnant leach solution (PLS).

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Residence Time Calculator Online Tools Cytiva

Residence Time Calculator. Calculate the residence time from given flow velocity and bed height. Fill Flow velocity together with bed height and hit the "Calculate" button to calculate the Residence time. Hit "Reset" button to clear the fields.

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Determination of Flow Structure in a G Leaching Tank by

Experimental residence time distribution (RTD) measurement and computational fluid dynamics (CFD) simulation are the best methods to study the hydrodynamics of process flow systems. However, CFD approach leads to better understanding of the flow structure and extent of mixing in stirred tanks. In the present study, CFD models were used to simulate the flow in an industrial g leaching tank.

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ASSESSING THE PERFORMANCE AND CAPACITY OF MATTE

An assessment of the capacity of the leaching tanks and autoclaves was performed using a predictive model within the AweSym flowsheet simulator. The model is described, and the results of the application of the model to a where t is the mean residence time, rs is the rate of shrinkage of the particles (leaching kinetics)

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v118n5a2 Test work to examine the potential for improving

carboninpulp leaching, and electrowinning. Figure 1 shows the layout of the leach section, which consists of one preoxidation tank and eight leach tanks with a total residence time of approximately 18 hours. The throughput is 200 t/h with the feed at 75% passing 75 μm and pulp density 50% solids. Oxygen is injected into the tanks to

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CIL G Mining Solution Mineral Processing

Sufficient residence time is provided in each tank to facilitate the leaching. Carbon particles are suspended in the tanks to simultaneously adsorb g from cyanide solution. Screens are installed in each tank to prevent carbon transfer along with the ore.

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Leaching and adsorption circuits for better metal extraction

The sizing of the tanks is calculated based on the time required to completely leach the ore, usually 2472 hours. The tanks are configured in stages and can be configured in cascade orientation making use of gravity slurry flow or in an active carousel configuration where the slurry is effectively pump from tank to tank.

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Residence time distribution in continuous stirred tank

While the mean residence time can be calculated as t¯ = tE(t)dt. (29) 0 The E( ) has been calculated using Eq. (27) and converted to E(t) Fig. 6. Influence of exchange flow ratio on exit age distribution in a stirred tank by dividing mean residence time of the electrolyte.

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CIL g processing plant CIL processing plant for sale

Before leaching, the pulp is passed through a linear vibrating screen to ensure removal of trash materials. This is done to minimize screen blocking in the adsorption section. After ore pulp prescreening, the pulp flows through a cascade of well mixed adsorption tanks, typically 68 in number. The pulp residence time is about one hour in each

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