CN1303230C - Pressure oxidation leaching method for nickel-cobalt oxide ore - Google Patents

Pressure oxidation leaching method for nickel-cobalt oxide ore Download PDF

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CN1303230C
CN1303230C CNB2005100732477A CN200510073247A CN1303230C CN 1303230 C CN1303230 C CN 1303230C CN B2005100732477 A CNB2005100732477 A CN B2005100732477A CN 200510073247 A CN200510073247 A CN 200510073247A CN 1303230 C CN1303230 C CN 1303230C
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nickel
cobalt oxide
cobalt
oxide ore
ore
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CN1676634A (en
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黄振华
何德礼
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Beijing General Research Institute of Mining and Metallurgy
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Beijing General Research Institute of Mining and Metallurgy
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Abstract

The invention discloses a pressure oxidation leaching method of nickel-cobalt oxide ore, which comprises the process flows of grinding nickel-cobalt oxide ore pulp, adding sulfur powder pulp or sulfide ore concentrate pulp, carrying out high-pressure kettle oxidation reaction, self-evaporating a flash tank, adding a coagulant, carrying out 7-stage countercurrent dense washing, extracting nickel and cobalt, comprehensively recovering magnesium sulfate and the like, and has the advantage of leaching nickel-cobalt metal and related components with high leaching rate.

Description

A kind of pressure oxidation leaching-out method for nickel-cobalt oxide ore
Affiliated technical field
The present invention relates to chemical industry metallurgical refinement technique field, relate to a kind of pressure oxidation leaching-out method for nickel-cobalt oxide ore specifically.
Background technology
In current chemical industry metallurgical refinement technique field, from nickel-cobalt oxide ore, pass through the traditional technology method of pressurized acid leaching technology also in widespread use, as everyone knows, nickel-cobalt oxide ore has different grades and gangue type, can adopt pyrometallurgy and hydrometallurgical processes to handle respectively, refine and produce ferronickel, sintering oxidation nickel, nickelous sulfide cobalt mixture, nickel cobalt hydroxide and rich nickel cobalt leach liquor, produce pure metal, metal powder or its esters by refining again.The oxidized ore that pyrometallurgy is handled requires nickeliferous higher, and the nickel-cobalt oxide ore raw material of handling as rotary kiln electric furnace reduction method and rotary kiln for directly reducing method contains Ni 〉=1.5%, MgO<32%, Fe>10%, output ferronickel.The method of hydrometallurgical process nickel-cobalt oxide ore has ammonia leaching process-use NH 3And CO 2For leaching agent and pressurized acid leaching method-directly adopt sulfuric acid are leaching agent, general nickel-cobalt oxide ore raw material contains Ni>1%.Ammonia leaching process can suppress the leaching of MgO, so suitable treatment contains the nickel-cobalt oxide ore of MgO>10%, but the nickel cobalt leaching yield of this method is lower, and the nickel leaching yield is generally 75~85%, cobalt leaching yield≤50%.Sulfuric acid leaching contains the higher ore of MgO because of economic reasons is not suitable for handling usually, and this method requires gangue MgO<10% in the raw material, be generally 0.5~6%, but this method nickel cobalt leaching yield is very high, usually Ni 〉=95%, Co 〉=92%.
Nineteen fifty-nine, U.S. free port sulphur company built the oxidized ore that Mao A factory adopts pressurized acid leaching art breading Ni1.3~1.5%, Co0.11~0.13%, Mg0.4~0.8% at Cuba hair A Wan, this factory set up joint venture in 1994 with the special company of Canadian Buddhist relics, and the nickel leaching yield improves 96% by 94%.Australia had built Mu Linmulin factory in succession when 20th century, art was to the turn of the century beginning of this century, Cowes factory and Bu Long factory, adopt sulfuric acid pressurized acid leaching art breading nickel-cobalt oxide ore, the product of each factory is all inequality, be respectively nickel cobalt sulfide, oxyhydroxide and rich nickel, rich cobalt liquid, produce metal products by refining, leach the nickel cobalt though adopt traditional sulfuric acid pressurized acid leaching art breading nickel-cobalt oxide ore to reach, and then produce metal products by refining, but the shortcoming that exists is, need in still, directly add sulfuric acid, need to build supporting vitriol works sulfuric acid is provided, strengthened the investment of founding the factory, also will produce adverse influence to environment, and also need in process of production with the high pressure steam supplementary heating to keep best extraction temperature, also cause production cost to improve, how to solve the shortcoming that above-mentioned processing method exists, make pressure oxidation leaching-out method for nickel-cobalt oxide ore can simplify technical process, thereby reduce investment outlay and production energy consumption, reducing production costs, is current present technique field problem anxious to be solved.
Summary of the invention:
The purpose of this invention is to provide a kind of pressure oxidation leaching-out method for nickel-cobalt oxide ore, this method can be simplified technical process, thereby reduces investment outlay and production energy consumption, reduces production costs, also can solve environmental pollution problems, simultaneously also can be to the byproduct comprehensive reutilization that occurs in the production process.
In order to achieve the above object, the present invention adopts following technical scheme, a kind of pressure oxidation leaching-out method for nickel-cobalt oxide ore, comprise grinding the nickel-cobalt oxide ore ore pulp, adding the SULPHUR POWDER slurry that specifically processing step is as follows or/and sulphide concentrate slurry, autoclave pressure oxidation leaching, flash drum self-evaporatint n., add flocculation agent, the dense washing of multi-stage countercurrent, extract technologies such as nickel cobalt and comprehensive reclaim(ed) sulfuric acid magnesium:
(1). when grinding the nickel-cobalt oxide ore ore pulp, nickel-cobalt oxide ore added grind to form ore pulp behind the water and send into the pulp pre-heating device, or the underflow after nickel laterite classification, the thickener dehydration is directly sent into the pulp pre-heating device;
(2). add the SULPHUR POWDER slurry or/and the sulphide concentrate slurry, the nickel-cobalt oxide ore ore pulp is preheating to 120-180 ℃ of temperature in the pulp pre-heating device after, add the SULPHUR POWDER slurry or/and add the sulphide concentrate slurry, the weight ratio of adding SULPHUR POWDER slurry and sulphide concentrate slurry is 1: 1-3;
(3). nickel-cobalt oxide ore ore pulp that will be after preheating and SULPHUR POWDER slurry are or/and the sulphide concentrate slurry pumps in the autoclave simultaneously, generate sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach the composition of part magnesium, calcium, aluminium, chromium, iron, manganese in nickel cobalt and the gangue and keep necessary free acid, the chemical reaction heat content that oxidizing reaction produces rises the temperature of ore pulp in the still automatically and is retained to the nickel cobalt and leaches required temperature, is 230~270 ℃;
(4). ore pulp is finished oxidizing reaction and gone out still in autoclave after, produce low pressure steam by flash drum, this low pressure steam is sent the pulp pre-heating device back to;
(5). the ore pulp after the flash distillation carries out the dense washing of 5-8 stage countercurrent after adding flocculation agent, the leaching tailings after obtaining nickel cobalt leach liquor after the liquid-solid separation and washing;
(6) the liquid-solid nickel cobalt leach liquor that separates the back gained can adopt existing various chemical precipitation method to obtain nickel cobalt mixed sulfides, oxyhydroxide, or adopt solvent extration to obtain rich nickel cobalt strip liquor, for being refined into metal products and high-purity salt, the comprehensive sal epsom that reclaims wherein of evaporative crystallization method of the mother liquor behind the separating nickel cobalt.
In the above-mentioned described step (2), when starching, independent interpolation sulphide concentrate can mix the common preheating in back with the nickel-cobalt oxide ore slurry;
The ratio of adding the weight percent of SULPHUR POWDER slurry amount and nickel-cobalt oxide ore ore pulp amount in the above-mentioned described step (2) is 6.5-40: 100.
The ratio of adding the weight percent of sulphide concentrate slurry amount and nickel-cobalt oxide ore ore pulp amount is 16-108: 100.
The ratio of adding SULPHUR POWDER slurry and sulphide concentrate slurry mixed ore pulp amount and nickel-cobalt oxide ore slurry amount weight percent is 10-80: 100.
Add the sulphide concentrate slurry in the above-mentioned described step (2) and comprise concentrate slurries such as containing cobalt sulphide ores, nickel pyrrhotite, magnetic pyrite or pyrite.
Nickel cobalt extraction time described in the above-mentioned described step (3) is: when temperature in the kettle was 230~270 ℃, the extraction time of various nickel-cobalt oxide ores was 30~150min.
The oxygen partial pressure that charges into described in the above-mentioned described step (3) in the still is 0.5~1.0MPa.
The temperature of reaction of the maintenance the best described in the above-mentioned described step (3) is taken away unnecessary heat by the heat exchange method of chuck, or changes pure oxygen into waste gas that oxygen enrichment discharges by still and take away unnecessary heat.
The kind of the interpolation flocculation agent described in the above-mentioned described step (5) is a polyacrylamide, and its addition is 5-100g/t.
In above-mentioned described step (1), when the thickener underflow after adopting nickel laterite classification dehydration was raw material, the weight ratio that the thickener underflow pulp density requires was 28-36%, and can directly replace nickel-cobalt oxide ore is raw material, saved the ore grinding step, leached the nickel cobalt and come to the same thing.
The invention belongs to the hydrometallurgy lixiviation process, it is leaching agent that this method does not directly adopt sulphate reagent, so need not in still, directly to add sulfuric acid, but in going into the ore pulp of still, the nickel-cobalt oxide ore preheating adds the SULPHUR POWDER slurry simultaneously or/and the sulphide concentrate slurry, ore pulp is starched or/and the sulphide concentrate slurry pumps in the autoclave simultaneously through being preheated to required temperature and SULPHUR POWDER, at this moment elementary sulfur (S 0) or vulcanised ore concentrate (S 2-Or S 0+ S 2-) sulfuric acid of oxidizing reaction generation faster takes place in gas-liquid-solid three-phase with the oxygen that charges in the still, meanwhile sulfuric acid of Sheng Chenging and nickel-cobalt oxide ore react, and the nickel cobalt in the leaching oxidized ore, the relevant composition in the gangue and keep the required free acid of nickelic cobalt leaching yield, S 0Or S 2-Chemical reaction heat content that oxidizing reaction produced and Dilution of sulphuric acid heat content make ore pulp be risen automatically by the temperature of going into still and are retained to the nickel cobalt and leach required optimum temps, to obtain the nickel cobalt of high leaching yield.Optimum temps in the reactor is by sulphur (S 0, S 2-) be oxidized to the heat content that discharged of acid and the dilution heat content is kept, need not during normal operation directly or indirectly to heat ore pulp with high pressure steam, only need when each the driving, to use direct preheating ore pulp of steam and equipment.
And various nickel-cobalt oxide ores when leaching required sulfur content be different, the mole number basically identical that the required acid of the sulfur content of its interpolation and conventional pressurized acid leaching nickel-cobalt oxide ore is measured.Corresponding the increasing of sulfur content of when alkaline earth metal content is higher in the nickel-cobalt oxide ore, being added, this moment sulphur be oxidized to acid chemical heat content and Dilution of sulphuric acid heat also increase, for the maintenance heat balance can reasonably keep the temperature of reaction of medium in the still by adjusting still slurry temperature and the distribution that charges into each chamber oxygen amount.In addition can unnecessary heat be taken away by suitable heat exchange method (as the chuck cooling) by-product low-pressure steam in case of necessity, also pure oxygen can be changed into oxygen enrichment and take away unnecessary heat by the waste gas of discharging by still.
Contain the high nickel-cobalt oxide ore of magnesium and leach through the pressure oxidation self-heating, the mother liquor that leach liquor reclaims behind the nickel cobalt need consider comprehensively to reclaim by-product MgSO 4.6H 2The O goods.But because the density of leach liquor reaches 1.2g/cm 3Ore pulp need guarantee that liquid-solid separation successfully carries out by adding corresponding flocculation agent, the liquid-solid nickel cobalt leach liquor that separates the back gained can adopt existing various chemical precipitation method to obtain nickel cobalt mixed sulfides, oxyhydroxide, also can adopt solvent extration to obtain rich nickel cobalt strip liquor, for being refined into metal products and high-purity salt.When oxidized ore contains magnesium when higher, the mother liquor behind the separating nickel cobalt can be with the comprehensive sal epsom crystalline product that reclaims wherein of conventional evaporative crystallization method.
Add the processing method of sulphur or sulphide concentrate pressure oxidation leaching nickel cobalt with nickel-cobalt oxide ore owing to adopted the above, make the present invention save facility and process cost that vitriolic transported and be conveyed into still, also save the investment and the productive expense of building vitriol works, and can reduce pollution to environment, help environment protection; Only need when the flow process running is produced during driving, to use steam preheating equipment and ore pulp, do not need during ordinary production with high pressure steam supplementary heating ore pulp, construction scale and the process cost that can dwindle boiler greatly; And need not directly add sulfuric acid to autoclave, the fouling of the corrosion that helps slowing down each compartment material in the still during with the ore pulp leaching; When adopt adding vulcanised ore concentrate, comprehensively reclaim valuable metal wherein incidentally, in addition, when the nickel-cobalt oxide ore that leaches contains magnesium when high, comprehensive reclaim(ed) sulfuric acid magnesium crystalline product the mother liquor after reclaiming the nickel cobalt again.
Can find out significantly that by the above the present invention optimizes the process quilt of the conventional press acidleach nickel-cobalt oxide ore of existing production application expeditiously.Can reduce investment significantly, reduce operator, save energy consumption, improve environment protection, reduce production costs, also can enlarge the adaptability scope of hydrometallurgy, and can other compositions in the raw material be fully utilized the nickel-cobalt oxide ore composition.
Description of drawings:
Fig. 1 is a technical process schematic block diagram of the present invention
Embodiment:
Below in conjunction with accompanying drawing in detail the present invention is described in detail, Fig. 1 clearly demonstrates technical process of the present invention, a kind of pressure oxidation leaching-out method for nickel-cobalt oxide ore, comprise grinding the nickel-cobalt oxide ore ore pulp, adding the SULPHUR POWDER slurry that its concrete process flow steps is as follows or/and sulphide concentrate slurry, autoclave pressure oxidation leaching, flash drum self-evaporatint n., add technologies such as flocculation agent, the dense washing of multi-stage countercurrent, extraction nickel cobalt and comprehensive reclaim(ed) sulfuric acid magnesium:
Example 1:
(1). grind the nickel-cobalt oxide ore ore pulp, with nickel-cobalt oxide ore 108.3g, composition is (%wt) Ni1.70, Co0.046, Fe11.2, MgO27.0, Si35.22; Add and grind to form ore pulp behind the water and send into the pulp pre-heating device;
(2). add the SULPHUR POWDER slurry, the nickel-cobalt oxide ore ore pulp is preheated to 180 ℃ of temperature in the pulp pre-heating device after, add the SULPHUR POWDER slurry, addition is that the SULPHUR POWDER slurry contains elementary sulfur 37.7g, water 600ml;
(3). the nickel-cobalt oxide ore ore pulp that has added the SULPHUR POWDER slurry after preheating is pumped in the autoclave, oxygenation in still when temperature is 180 ℃ in autoclave, oxygen partial pressure is 0.7MPa, stirring linear speed in the still is 3.0m/s, the elementary sulfur of SULPHUR POWDER slurry generates sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach corresponding composition and the necessary free acid of maintenance in nickel cobalt and the gangue, oxidizing reaction produces and the temperature of maintenance is 250 ℃, and the time of leaching the nickel cobalt is 60min;
(4). ore pulp is finished oxidizing reaction and gone out still in autoclave after, produce low pressure steam by flash drum, this low pressure steam is sent the pulp pre-heating device back to, and steam more than needed can carry out other comprehensive utilizations;
(5). the ore pulp after the flash distillation adds the polyacrylamide flocculation agent in the ratio of interpolation 30 grams per ton, carries out the dense washing of 7 stage countercurrents then, obtains nickel cobalt leach liquor after the liquid-solid separation;
The result is leached in check: leached mud contains Ni0.059%, Co0.044%, and MgO0.78%, leach liquor contains Ni3g/l, Co0.082g/l, Fe1.67g/l, MgO58.3g/l, pH0.63, ρ L=1.192g/cm 3By slag nickel leaching yield 98%, cobalt 94.6%, MgO98.4%.
(6) the liquid-solid nickel cobalt leach liquor that separates the back gained can adopt existing various chemical precipitation method to obtain nickel cobalt mixed sulfides, oxyhydroxide, also can adopt solvent extration to obtain rich nickel cobalt strip liquor, for being refined into metal products and high-purity salt, the mother liquor behind the separating nickel cobalt can be used the comprehensive sal epsom that reclaims wherein of evaporative crystallization method.
Embodiment 2:
(1). adopt the thickener underflow ore pulp after the nickel laterite classification is dewatered, nickel-cobalt oxide ore material amount 134.6g, composition are (%wt) Ni0.95, Co0.17, Fe42.2, Mg1.44, Mn1.23, Cr0.37, Al5.12 sends into the pulp pre-heating device after Si4.90 is direct;
(2). add the sulphide concentrate slurry, the nickel-cobalt oxide ore ore pulp is preheating to 180 ℃ of temperature in the pulp pre-heating device after, add cobalt sulphur concentrate 33.4g, it consists of Ni0.083%, Co0.14%, Cu0.36%, S37.42% adds water 600ml and mixes the common preheating in back with the nickel-cobalt oxide ore slurry;
(3). the nickel-cobalt oxide ore ore pulp that has added cobalt sulphur concentrate slurry after preheating is pumped in the autoclave, oxygenation in still when temperature is 180 ℃ in autoclave, oxygen partial pressure is 0.9MPa, stirring linear speed in the still is 3.0m/s, the elementary sulfur of cobalt sulphur concentrate pulp generates sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach corresponding composition and the necessary free acid of maintenance in nickel cobalt and the gangue, oxidizing reaction produces and the temperature of maintenance is 250 ℃, and the time of leaching the nickel cobalt is 42min;
Other steps such as embodiment 1.
The result is leached in check: leached mud contains Ni0.0032%, Co<0.005%, and leach liquor contains Ni2.44g/l, Co0.36g/l, Fe1.88g/l, pH0.58 is by slag nickel leaching yield 97.25%, cobalt 97.6%.
When a cobalt sulphur concentrate pulp that adds being changed into concentrate slurry such as nickel pyrrhotite, magnetic pyrite or pyrite, processing step is constant, and its effect that leaches the nickel cobalt is identical.
Embodiment 3
(1). grind the nickel-cobalt oxide ore ore pulp, with nickel-cobalt oxide ore 168g, composition is (%wt) Ni0.95, and Co0.17, Fe42.2, Mg1.44, Mn1.23, Cr0.37, Al5.12, Si4.9 add and grind to form ore pulp behind the water and send into the pulp pre-heating device;
(2). add sulphide concentrate slurry and SULPHUR POWDER slurry, the nickel-cobalt oxide ore ore pulp is preheating to 180 ℃ of temperature in the pulp pre-heating device after, add cobalt sulphur concentrate pulp 80.7g, composition is: Ni0.083%, Co0.14%, Cu0.36%, S37.42%, add SULPHUR POWDER slurry 30.2g again, add water 600ml and mix the common preheating in back with cobalt sulphur concentrate pulp and nickel-cobalt oxide ore slurry;
(3). the nickel-cobalt oxide ore ore pulp that has added cobalt sulphur concentrate slurry and SULPHUR POWDER slurry mixed pulp after preheating is pumped in the autoclave, oxygenation in still when temperature is 180 ℃ in autoclave, oxygen partial pressure is 1.0MPa, stirring linear speed in the still is 3.0m/s, the elementary sulfur of cobalt sulphur concentrate pulp generates sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach corresponding composition and the necessary free acid of maintenance in nickel cobalt and the gangue, oxidizing reaction produces and the temperature of maintenance is 250 ℃, and the time of leaching the nickel cobalt is 120min;
Other steps such as embodiment 1 and embodiment 2.
The result is leached in check: leached mud contains Ni0.057%, Co0.009%, and leach liquor contains Ni4.49g/l, and Co0.30g/l is by slag nickel leaching yield 97.2%, cobalt 93.12%.
Embodiment 4
(1). adopt the thickener underflow ore pulp after the nickel laterite classification is dewatered, nickel-cobalt oxide ore 168g, material amount 134.6g, composition are (%wt) Ni0.95, Co0.17, Fe42.2, Mg1.44, Mn1.23, Cr0.37, Al5.12, Si4.90 directly send into the pulp pre-heating device;
(2). add the SULPHUR POWDER slurry, the nickel-cobalt oxide ore ore pulp is preheated to 180 ℃ of temperature in the pulp pre-heating device after, add the SULPHUR POWDER slurry, addition is that the SULPHUR POWDER slurry contains elementary sulfur 16.4g, adds water 600ml;
(3). the nickel-cobalt oxide ore ore pulp that has added the SULPHUR POWDER slurry after preheating is pumped in the autoclave, oxygenation in still when temperature is 180 ℃ in autoclave, oxygen partial pressure is 0.6MPa, stirring linear speed in the still is 3.0m/s, the elementary sulfur that bores the sulphur concentrate pulp generates sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach corresponding composition and the necessary free acid of maintenance in nickel cobalt and the gangue, oxidizing reaction produces and the temperature of maintenance is 250 ℃, and the time of leaching the nickel cobalt is 60min;
Other steps such as embodiment 1.
The result is leached in check: leached mud contains Ni0.027%, Co<0.005%, and leach liquor contains Ni3.0g/l, Co0.33g/l, Fe2.82g/l, pH0.51.By slag nickel leaching yield 97.6%, cobalt 97.5%.
Embodiment 5
Its composition of raw material 168g is (%wt) Ni.47, Co0.1, Fe37.2, Mg1.44, Mn0.77, Cr0.22, Al4.04, Si7.79 adds elementary sulfur 17.4g and adds water 600ml, 1% defoamer (XP-1) 0.24ml, in mechanical stirring kettle, stir linear speed 3m/s, in 180 ℃ of oxygenations of temperature, oxygen partial pressure 0.5~1MPa leaches 90min down at 250 ℃.
Leach the result: leached mud contains Ni0.052%, Co<0.005%, and leach liquor contains Ni4.31g/l, Co0.17g/l, Fe2.52g/l, pH0.51.By slag nickel leaching yield 96.8%, cobalt 95.5%.
(1). adopt the thickener underflow ore pulp after the nickel laterite classification is dewatered, the heavy 168g of nickel-cobalt oxide ore material, composition is (%wt) Ni1.47, Co0.1, Fe37.2, Mg1.44, Mn0.77, Cr0.22, Al4.04, Si7.79 directly send into the pulp pre-heating device;
(2). add the SULPHUR POWDER slurry, the nickel-cobalt oxide ore ore pulp is preheated to 180 ℃ of temperature in the pulp pre-heating device after, add the SULPHUR POWDER slurry, addition is that the SULPHUR POWDER slurry contains elementary sulfur 17.4g, adds water 600ml;
(3). the nickel-cobalt oxide ore ore pulp that has added the SULPHUR POWDER slurry after preheating is pumped in the autoclave, oxygenation in still when temperature is 180 ℃ in autoclave, oxygen partial pressure is 0.7MPa, stirring linear speed in the still is 3.0m/s, the elementary sulfur of cobalt sulphur concentrate pulp generates sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach corresponding composition and the necessary free acid of maintenance in nickel cobalt and the gangue, oxidizing reaction produces and the temperature of maintenance is 250 ℃, and the time of leaching the nickel cobalt is 90min;
Other steps such as embodiment 1.
The result is leached in check: leached mud contains Ni0.052%, Co<0.005%, and leach liquor contains Ni4.31g/l, Co0.17g/l, Fe2.52g/l, pH0.51.By slag nickel leaching yield 96.8%, cobalt 95.5%.

Claims (9)

1. pressure oxidation leaching-out method for nickel-cobalt oxide ore, comprise grinding the nickel-cobalt oxide ore ore pulp, adding the SULPHUR POWDER slurry that specifically processing step is as follows or/and sulphide concentrate slurry, autoclave pressure oxidation leaching, flash drum self-evaporatint n., add flocculation agent, the dense washing of multi-stage countercurrent, extract technologies such as nickel cobalt and comprehensive reclaim(ed) sulfuric acid magnesium:
(1). when grinding the nickel-cobalt oxide ore ore pulp, nickel-cobalt oxide ore added grind to form ore pulp behind the water and send into the pulp pre-heating device, or the underflow after nickel laterite classification, the thickener dehydration is directly sent into the pulp pre-heating device;
(2). add the SULPHUR POWDER slurry or/and the sulphide concentrate slurry, the nickel-cobalt oxide ore ore pulp is preheating to 120-180 ℃ of temperature in the pulp pre-heating device after, add the SULPHUR POWDER slurry or/and add the sulphide concentrate slurry, the weight ratio of adding SULPHUR POWDER slurry and sulphide concentrate slurry is 1: 1-3;
(3). nickel-cobalt oxide ore ore pulp that will be after preheating and SULPHUR POWDER slurry are or/and the sulphide concentrate slurry pumps in the autoclave simultaneously, generate sulfuric acid with the oxygen generation oxidizing reaction that charges in the still, sulfuric acid reacts with nickel-cobalt oxide ore simultaneously, leach part magnesium in nickel cobalt and the gangue, calcium, aluminium, chromium, iron, manganese composition and keep necessary free acid, the chemical reaction heat content that oxidizing reaction produces rises the temperature of ore pulp in the still automatically and is retained to the nickel cobalt and leaches required temperature, is 230~270 ℃;
(4). ore pulp is finished oxidizing reaction and gone out still in autoclave after, produce low pressure steam by flash drum, this low pressure steam is sent the pulp pre-heating device back to;
(5). the ore pulp after the flash distillation carries out the dense washing of 5-8 stage countercurrent after adding flocculation agent, obtains nickel cobalt leach liquor after the liquid-solid separation;
(6) the liquid-solid nickel cobalt leach liquor that separates the back gained adopts chemical precipitation method to obtain nickel cobalt mixed sulfides, oxyhydroxide, or adopt solvent extration to obtain rich nickel cobalt strip liquor, for being refined into metal products and high-purity salt, the comprehensive sal epsom that reclaims wherein of evaporative crystallization method of the mother liquor behind the separating nickel cobalt.
2. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1, it is characterized in that: in the above-mentioned described step (1), when the thickener underflow after the employing nickel laterite classification dehydration was raw material, the weight ratio that the thickener underflow pulp density requires was 28-36%.
3. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: in the above-mentioned described step (2), mix back preheating jointly with the nickel-cobalt oxide ore slurry when independent interpolation sulphide concentrate is starched;
4. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: the weight ratio of adding SULPHUR POWDER slurry amount and nickel-cobalt oxide ore ore pulp amount in the above-mentioned described step (2) is 6.5-40: 100; The weight ratio of adding sulphide concentrate slurry amount and nickel-cobalt oxide ore ore pulp amount is 16-108: 100; Adding SULPHUR POWDER slurry and sulphide concentrate slurry mixed ore pulp amount and nickel-cobalt oxide ore slurry amount weight ratio is 10-80: 100.
5. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: add the sulphide concentrate slurry in the above-mentioned described step (2) and comprise that containing cobalt sulphide ores, nickel pyrrhotite, magnetic pyrite or sulphur ore starches.
6. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1, it is characterized in that: the time that nickel cobalt described in the above-mentioned described step (3) leaches, the extraction time of various nickel-cobalt oxide ores was 30~150min under 230~270 ℃ of extraction temperatures in still.
7. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: the oxygen partial pressure that charges into described in the above-mentioned described step (3) in the still is 0.5~1.0MPa.
8. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: the temperature of reaction that keeps described in the above-mentioned described step (3), by the heat exchange method of chuck unnecessary heat is taken away; Or change pure oxygen into waste gas that oxygen enrichment discharges by still and take away unnecessary heat.
9. pressure oxidation leaching-out method for nickel-cobalt oxide ore according to claim 1 is characterized in that: the kind of the interpolation flocculation agent described in the above-mentioned described step (5) is a polyacrylamide, and its addition is 5-100g/t.
CNB2005100732477A 2005-06-03 2005-06-03 Pressure oxidation leaching method for nickel-cobalt oxide ore Expired - Fee Related CN1303230C (en)

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Publication number Priority date Publication date Assignee Title
CN100340680C (en) * 2006-04-25 2007-10-03 东北大学 Method for inhibiting scale-forming during the process of leaching nickle from nickle-contg. laterate by sulfuric acid
CN101245414B (en) * 2007-02-15 2011-12-21 邓彤 Method for extracting metal from laterite mine
CN101328537B (en) * 2007-06-18 2010-04-21 中国恩菲工程技术有限公司 Process for comprehensive recovery nickel, copper, cobalt, sulfur and magnesium from high magnesium and nickle ore concentrate
FI123884B (en) 2011-11-08 2013-11-29 Outotec Oyj A process for dissolving a sulphidic metal concentrate
CN103725899A (en) * 2013-12-13 2014-04-16 金川集团股份有限公司 Method for leaching Cuba nickel-cobalt raw material
CN103966432A (en) * 2014-05-09 2014-08-06 昆明理工大学科技产业经营管理有限公司 Method for leaching nickel and molybdenum from amorphous nickel-molybdenum sulfide mineral by oxidative conversion
CN105568000A (en) * 2016-02-03 2016-05-11 广东佳纳能源科技有限公司 Combined high-pressure acid leaching method for cobalt containing sulfide and heterogenite
CN106048216B (en) * 2016-06-22 2018-07-17 荆门市格林美新材料有限公司 The method of heterogenite leaching cobalt
CN106222404B (en) * 2016-09-23 2019-04-09 中国恩菲工程技术有限公司 The recovery system of valuable metal
CN107058732B (en) * 2017-05-29 2019-03-01 新疆新鑫矿业股份有限公司阜康冶炼厂 A kind of nickel minerals pressure leaching method
CN108728670A (en) * 2018-06-21 2018-11-02 柴迪汉 A kind of cobalt leaching polypropylene-base leachate and preparation method thereof
CN112553478A (en) * 2020-12-02 2021-03-26 金川集团镍盐有限公司 Method for quickly leaching nickel hydroxide cobalt sulfuric acid system
CN116516171A (en) * 2023-04-03 2023-08-01 西安陕鼓动力股份有限公司 Method for preheating, temperature-reducing and pressure-reducing ore pulp in wet acid leaching of laterite-nickel ore
CN116356157A (en) * 2023-04-03 2023-06-30 西安陕鼓动力股份有限公司 Device and method for treating ore pulp before and after laterite-nickel ore wet acid leaching reaction

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5855858A (en) * 1993-07-29 1999-01-05 Cominco Engineering Services Ltd. Process for the recovery of nickel and/or cobalt from an ore or concentrate
CN1352308A (en) * 2001-11-09 2002-06-05 北京矿冶研究总院 Method for extracting nickel from nickel sulfide material with low copper content

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5855858A (en) * 1993-07-29 1999-01-05 Cominco Engineering Services Ltd. Process for the recovery of nickel and/or cobalt from an ore or concentrate
CN1352308A (en) * 2001-11-09 2002-06-05 北京矿冶研究总院 Method for extracting nickel from nickel sulfide material with low copper content

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