Classifications

• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
  • C22B59/00—Obtaining rare earth metals
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
  • C01F11/00—Compounds of calcium, strontium, or barium
  • C01F11/46—Sulfates
  • C01F11/466—Conversion of one form of calcium sulfate to another
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
  • C01F11/00—Compounds of calcium, strontium, or barium
  • C01F11/46—Sulfates
  • C01F11/468—Purification of calcium sulfates
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
  • C01F17/00—Compounds of rare earth metals
  • C01F17/20—Compounds containing only rare earth metals as the metal element
  • C01F17/282—Sulfates
• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
  • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
  • C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
  • C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
  • C22B3/08—Sulfuric acid, other sulfurated acids or salts thereof
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
  • C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
  • C01P2006/62—L* (lightness axis)
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
  • C01P2006/63—Optical properties, e.g. expressed in CIELAB-values a* (red-green axis)
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
  • C01P2006/64—Optical properties, e.g. expressed in CIELAB-values b* (yellow-blue axis)
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/80—Compositional purity
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• the present invention relates to a rare earth-containing calcium sulfate treatment method comprising the steps of:
• Such a method is for example known from CN 10197688.
• a phosphogypsum containing rare earths resulting from a phosphated rock treatment for the production of phosphoric acid, is treated with sulfuric acid. Then, the lixivation liquor is brought into contact with calcium nitrate, so as to maintain the rare earths in nitrate form in the liquid phase.
• the phosphogypsum may be a calcium sulfate dihydrate or hemihydrate resulting from a primary or secondary filtration.
• the yields obtained in the examples mentioned are less than 50% relative to the initial rare earth content and the precipitation of rare earths with calcium nitrate makes it possible to reach precipitation yields of between 80 and 90%.
• phosphogypsum in the present context is meant a calcium sulfate having the formula CaSO 4 . xH 2 0 wherein x is 0, 1 ⁇ 2 or 2, derived from phosphate rocks.
• the phosphogypsum is treated with sulfuric acid and optionally with a soluble ammonium salt. Then hydrofluoric acid or soluble fluoride is added to the leach liquor to produce a rare earth fluoride that precipitates and thus facilitates its recovery.
• RU2158317 Also known from RU2158317 is a process in which a phosphogypsum is treated with a leach solution to obtain a rare earth-containing sulfuric acid liquor.
• the rare earth-containing sulfuric acid liquor is then neutralized with a magnesium solution in the form of magnesium oxide or magnesium carbonate or a combined compound thereof for example in the form of hydromagnesite.
• WO2011008137 also discloses a process for extracting rare earths from phosphogypsum by a leaching step using a sulfuric acid and a nitric acid. Then, the rare earths are recovered using a cation exchange resin.
• Jarosinski et al. Journal of Alloys and Compounds, October 1993 also discloses the extraction of rare earths from phosphogypsum.
• phosphogypsum hemihydrate is leached with 10% concentrated sulfuric acid and at a temperature between 0 and 10 ° C, which of course requires cooling.
• calcium sulphate hemihydrate phosphogypsum hemihydrate
• the ripening phase of the hemihydrate to dihydrate is simultaneous with the extraction of rare earths during leaching.
• the phosphogypsum obtained after lixtviation is disclosed as being sufficiently pure to produce plaster by direct heat treatment.
• this process nevertheless remains constraining in what it requires to provide cooling during leaching, typically exothermic step and requires a residence time of 6 hours.
• the object of the invention is to overcome the drawbacks of the state of the art by providing a process which makes it possible to carry out the extraction of the rare earths in a manner entirely compatible with the production of phosphoric acid and which makes it possible to achieve extraction of high rare earths and improved quality of calcium sulphates obtained and which is simple and relatively ecological in its implementation.
• a method as indicated at the beginning further comprising, prior to said leaching, a calcium sulphate hemihydrate processing step containing said rare earths with crystallization of calcium sulphate dihydrate by collecting residual water and / or residual moisture.
• the calcium sulphate dihydrate used as a leaching substrate is not, in the process according to the invention, a calcium sulphate dihydrate directly from a separation step or a hemihydrate, but a sulphate of calcium from slow maturation of calcium sulphate hemihydrate by residual water uptake or residual moisture to crystallize as a calcium sulfate dihydrate.
• Calcium sulphate hemihydrate is stored in piles. These heaps are impermeable to ambient humidity and therefore the calcium sulphate hemihydrate can not capture the water from the atmosphere, but only the residual moisture from the filter cake resulting from the separation between phosphogypsum hemihydrate and the liquid phase during the production of phosphoric acid.
• the calcium sulfate dihydrate thus obtained according to the invention is in fact considered to be a perfect calcium sulphate in which the impurities which may be present are expelled during the very slow crystallization in the dihydrate form which takes place during the storage in piles by collecting residual moisture or residual water.
• the rare earth extraction yield relative to the initial calcium sulphate content is at least 80%.
• the calcium sulphate thus obtained after extraction of the rare earths, has a higher degree of purity, not only because it no longer contains rare earths, but also because it is depleted in contaminating compounds such as Na 2 0 and phosphate compounds.
• the process according to the invention does not require cooling during the leaching step which is typically exothermic.
• said sulfuric acid is a sulphuric acid solution having a concentration of 2 to 25%, preferably between 2 and 20%, more particularly between 5 and 18%, and most preferably between 7 and 12, or even between 8 and 10% by weight by weight relative to the total weight of the solution.
• This concentration proves to be the concentration providing the best leaching yields and thus makes it possible to optimize the yields of rare earth extraction from phosphogypsum.
• said calcium sulfate hemihydrate containing said rare earths is neutralized with a basic agent so as to provide a pH of between 4 and 12, preferably between 6.5 and 11.5.
• This basic agent may be, for example, soda or lime, such as lime in the form of live, extinct or milk of lime.
• the basic agent is quicklime.
• This neutralization step improves the rare earth extraction efficiency and improves the quality of calcium sulfate dihydrate obtained by slow maturation since the acidic conditions are neutralized before maturation and allows to achieve a complete rehydration of calcium sulfate.
• said lixiviation is carried out with stirring for a predetermined period of time ranging from 0.5 to 4 hours, preferably from 1 to 2 hours, which again makes it possible to obtain an optimal leaching yield between implementation cost. method, duration and stirring power and solubilization of rare earths in sulfuric acid.
• said leaching is preceded by a step of disintegrating the calcium sulphate dihydrate crystals formed during the maturation, in particular by means of a turbine rotating at 6000 rpm for a period of time of between 5 and 20 minutes. preferably at room temperature.
• disintegration in the sense of the present invention is meant a step of dividing crystalline aggregates of calcium sulfate dihydrate into finer particles under the effect of shear forces.
• the leaching temperature is between 10 and 70 o C, and is preferably the ambient temperature, such as between 20 and 30 ° C.
• the ratio of sulfuric acid / calcium sulfate matured during leaching is between 0.02 and 2.25, preferably from 0.15 to 0.35.
• the method further comprises a step of Saving said solid phase resulting from said separation with water or preferably with limed water, and optionally, a subsequent drying step of said solid phase.
• the washing water is recirculated to increase the yield of the extraction and reduce the dilution effect on the sulfuric acid concentration.
• said liquor containing said rare earths and sulfuric acid is recirculated a predetermined number of times. between 2 and 8 at said leaching step. From this, it follows that the sulfuric acid of the leach liquor is reused a predetermined number of times, which reduces the consumption of sulfuric acid relative to the amount of calcium sulfate dihydrate after slow maturation, namely in relation to the amount of calcium sulfate dihydrate to be treated.
• the sulfuric acid liquor is enriched in rare earths, which makes it possible to obtain a more profitable process and to facilitate the recovery steps of these downstream of the leaching.
• the invention also relates to a rare earth-containing sulfuric acid liquor obtained by the process according to the present invention.
• This sulfuric liquor can be either treated by conventional extraction processes in situ or marketed as such for rare earth operators. It can therefore be an intermediate product or a final product according to the present invention according to the needs of the market.
• rare earths are, once purchased by an operator, solubilized again in sulfuric acid, to make salts or other compounds. According to the present invention, it is possible to directly acquire the sulfuric liquor, either to obtain the desired final product, such as a rare earth compound, or to extract the rare earths and dispose of it.
• the present invention also provides that the rare earths can be extracted from the sulfuric acid liquor in situ to market them in the desired form rather than in the form of liquor.
• the sulfuric acid liquor according to the invention has a sulfuric acid concentration of between 2 and 25% by weight relative to the total weight of the sulfuric liquor.
• concentration of sulfuric acid is between 2 and 20%, more particularly between 5 and 18% and most preferably between 7 and 12, or even between 8 and 10% by weight.
• the sulfuric acid liquor according to the present invention has a rare earth concentration which is close to saturation (about 5000 ppm) relative to the total weight of the sulfuric liquor.
• the present invention also relates to a calcium sulfate dihydrate obtainable by the process according to present invention ie having a P 2 O content of residual s less than 0.05% by weight relative to the total weight of calcium sulphate .
• this content is very low and makes it possible to provide a calcium sulphate dihydrate with a high degree of purity.
• the P 2 0 5 is disruptive of setting time of cements and plasters and benefit from a phosphogypsum having a P 2 0 5 as low really is advantageous since the disruptive element content of the decision is reduced drastically.
• a conventional phosphogypsum present contents of P 2 0 5 of from 0.4 to 1% by weight relative to the total weight of calcium sulphate.
• said calcium sulfate dihydrate has a Na 2 0 content less than 500 ppm (or 0.05 wt%) relative to the total weight of calcium sulphate.
• the reduced Na 2 content limits efflorescence in the plaster.
• a conventional phosphogypsum has a Na 2 0 content of greater than 0.15%. After rare earth recovery leaching, the residual Na 2 0 content is less than 500 ppm, which corresponds to the limit set for use of calcium sulphate in gypsum board.
• plasterboards can also be manufactured with a higher phosphogypsum content according to the The present invention, which until now was problematic before further processing or mixing with calcium sulfates or gypsum purer, comprising no or little Na 2 0.
• the calcium sulfate dihydrate according to the present invention has a residual rare earth content of less than 20% by weight relative to the initial content in calcium sulphate (ie about 800 ppm).
• the calcium sulphate according to the invention has a particle size d50 of between 5 and 25 ⁇ m, preferably greater than 8 ⁇ m, more preferably greater than 10 ⁇ m, and preferably less than 20 ⁇ m. pm, more preferably less than 15 pm, which makes it possible to limit the particle size reduction steps in "plaster or cement" applications for which the particle size of the phosphogypsum should in all cases be reduced.
• the calcium sulphate according to the invention has a brightness Tappi with a reflectance of 457 nm of at least 86, preferably at least 87.
• the present invention thus allows a gain in whiteness which is positive for "plaster" applications downstream of the extraction process.
• the brightness at a reflectance of 457 nm for conventional phosophgypsis is about 84 while according to the present invention the Tappi whiteness can be as high as 87 and higher.
• the calcium sulphate according to the invention has a whiteness in the system L, a, b characterized by the following values: L> 95; a> -0.01, b ⁇ 1, 6.
• the present invention therefore relates to a calcium sulphate treatment process containing rare earths, preferably from the production of phosphoric acid from a phosphate rock.
• Such a rare earth-containing calcium sulfate can be obtained by a conventional method of reacting phosphate rock with sulfuric acid under conditions giving rise to crystallization of calcium sulfate dihydrate or gypsum ( CaSO 2 H 2 O).
• the gypsum slurry obtained in a first reactor can then be subjected, in a second reactor, to a maturation allowing magnification of the sulphate grains formed, and this to increase the filterability.
• the ripened slurry is then filtered to give a phosphoric acid having a P 2 0 5 content free of the order of 25 to 35% by weight.
• a hemihydrate is obtained, after having applied the conditions of the conventional method of forming a gypsum slurry, but by directly subjecting it to a mixture with sulphuric acid and optionally to a heating, without first separating the phosphoric acid production.
• the hemihydrate slurry obtained is filtered to give a very pure hemihydrate cake, but a filtrate formed from a mixture of phosphoric acid and sulfuric acid.
• the hemihydrate thus obtained is also a particularly advantageous candidate for the extraction of rare earths according to the process according to the invention.
• a rare earth-containing calcium sulfate may also be obtained for example by a process in which the phosphate rock is etched with sulfuric acid at particular temperatures and concentrations of P2O5 and / or SO3, a slurry of calcium sulphate under form of hemihydrate (CaSO 4 .1 / 2H 2 O) or anhydrite.
• the slurry obtained in a first reactor can then be subjected, in a second reactor, to a maturation allowing magnification of the calcium sulphate crystals formed, and this to increase filterability.
• the slurry matured in the second reactor is then filtered to obtain a phosphoric acid having a content of free P2O5 of the order of 25 to 35% by weight and a calcium sulfate hemihydrate cake.
• the method according to the present invention can also be applied to a calcium sulphate hemihydrate obtained from processes comprising a triple crystallization of calcium sulphate first in hemihydrate, then in dihydrate and finally again in hemihydrate (see US-A -4,588,570). It is also possible to obtain a calcium sulphate containing rare earths in the form of hemihydrate according to the teaching of the document WO 2011/067321. According to this process for the production of phosphoric acid, a first slurry of calcium sulphate crystals dihydrate in suspension. in an acidic aqueous phase is formed. The attack conditions are such that they provide for a substantially stoichiometric reaction between the sulfuric acid introduced and the calcium content.
• This first slurry is then directly subjected, in its entirety, to a conversion step which consists in heating it to a temperature greater than 90 ° C, which causes in a known manner a solubilization of gypsum crystals, release of P 2 O 5 co-crystallized in the gypsum during the etching step and recrystallization of calcium sulfate in the form of hemihydrate which has crystals of spherical shape and are of current size, for example having a d 50 of 60 ⁇ , which gives a filter cake having an excellent coefficient of filtration.
• This process is a process for the production of phosphoric acid by phosphate rock attack of poor quality by means of sulfuric acid which makes it possible to obtain a production phosphoric acid of good quality and a good extraction yield of P 2 O 5 to from the rock.
• This process comprises steps similar to those described above.
• a source of fluorine in a content of 1% to 5% by weight of F with respect to the P 2 O 5 contained in the phosphate rock is added to the first slurry.
• the calcium sulfate in the form of hemihydrate obtained in the second filter cake is also a good candidate for the rare earth recovery process according to the present invention.
• lanthanides also known as rare earths. This is particularly the case of phosphate Kola.
• calcium sulfate hemihydrate is obtained as a co-product of phosphoric acid.
• About 80% of all the lanthanides initially present in the phosphate rock are in the co-produced phosphogypsum.
• the calcium sulfate hemihydrate obtained according to any of the methods described above is then filtered and washed to be recovered from the mud or cake in which it is located.
• This calcium sulphate hemihydrate is in a preferred embodiment neutralized by a base, for example lime, in the form of quicklime.
• Calcium sulfate hemihydrate and neutralized is then stored in piles, usually in the open air to allow its maturation.
• the calcium sulfate hemihydrate thus stored absorbs moisture and / or residual water and converts into very pure calcium sulfate dihydrate crystals as mentioned above.
• This calcium sulphate thus matured is relatively pure, dry and can be easily handled and processed for later commercial recovery. It is from this calcium sulfate dihydrate and matured that the rare earths are extracted.
• the calcium sulfate dihydrate and matured is in the form of aggregates which are, before leaching, disintegrated by means of a turbine rotating at 6000 revolutions / minute for a period of time between 5 and 20 minutes, preferably at ambient temperature, which makes it possible to obtain fine particles of calcium sulphate dihydrate of small size.
• Fine particles of calcium sulfate containing said rare earths are then suspended with stirring for a predetermined period of time ranging from 0.5 to 4 hours in acid.
• sulfuric acid at 2 to 25% by weight and the rare earths are leached to end up in the aqueous phase, mainly.
• the solid phase formed of said calcium sulfate dihydrate is then separated from said liquid phase which is in the form of a liquid containing said rare earths and sulfuric acid.
• An example of appropriate separation is filtration.
• the solid phase resulting from said separation is then washed with water, and optionally dried.
• said liquor containing said rare earths and sulfuric acid is recirculated a predetermined number of times between 2 and 8 at said leaching step to concentrate the rare earth liquor.
• the gypsum thus obtained after leaching is purified in rare earths, but is also purified in other elements such as P 2 0 5 and Na 2 O which are disturbing for the production of plaster.
• a gypsum matured in the open air, after neutralization with quicklime (green gypsum) was analyzed and the analyzes were repeated on the gypsum obtained after leaching of the rare earths with 13% sulfuric acid. The results are shown in Table 1.
• the P 2 0 5 content (disruptive element of setting time of the cement and the plaster) of the leached gypsum is at least 10 times lower and the value Na 2 0 (efflorescence generator in the plaster ) is below the limit (SOOppm) set for use in plasterboard.
• all arsenic (As) is practically eliminated, the residual content of U 3 O s is practically zero and thorium is greatly reduced (10 times).
• the granulometry is also much finer which should also be an advantage and calcium sulphate gains in whiteness, gain of 0.8 on the "L" and 3.1 on the whiteness Tappi. Filtration here carried out under pressure makes it possible to maintain the residual water content below 10%.
• the sulfuric acid liquor according to the present invention was also analyzed for its rare earth content.
• Table 2 presents a typical analysis after 2 successive attacks and a backwash of the calcium sulphate matured and previously neutralized by quicklime with a 13% sulfuric acid.
• the lanthanide analyzes presented in Table 2 are performed by ICPAES (inductively coupled argon plasma atomic emission spectrophotometry analysis).
• the method according to the present invention therefore has a particularly high yield of rare earth or lanthanide extraction.
• the extraction yield is determined for each element and overall from the lanthanide content of the gypsum before (green gypsum) and after the sulfuric leaching which is multiplied by 100.
• the rare earth extraction was carried out by leaching with sulfuric acid under the conditions described above.
• the yields obtained are those presented in Table 3.
• ICPAES Inductively Coupled Argon Plasma Atomic Emission
• Gypsum Weigh + 1g of sample (dried at 250 ° C) and introduce it into a 100ml volumetric flask. Add 30 ml of nanopure water, 10 ml of HN0 3 and bring to a boil until completely dissolved. Cool the balloon gauged. Bring to the water with nanopure water, shake and filter on a 640 m MN filter.
• Sulfuric acid diluted Weigh + 10q of sample in a 100 ml volumetric flask. Add 30ml of nanopure water, 5ml of HCI, 5ml HN0 3 and bring to a boil. Cool the balloon gauged. Bring to volume with nanopure water, shake and filter on a 640 m MN filter.
• the Meinhard TR 50 C1 commercial fogger with cyclonic chamber is used in the JOBIN_YVON JY238 ULTRACE device
• Lanthanides Solution A (intermediate solution): Composition: 10 ppm Ho, Lu, Se, Tb, Tm; 20ppm Dy, Er, Eu, Yb; 5% HN0 3 .
• the high standard is also used as a control.
• a control standard is included at least once in the sample series.
• Exceeding an alert limit does not invalidate the results of the analyzes, but requires increased monitoring of the instrument. Exceeding a reject limit invalidates the results of the analyzes. The samples must be analyzed again after corrective action (s) and recalibration of the instrument.
• the analyzes of the lanthanides in the cake and the different filtrates are presented in Tables 2 and 3.
• the extraction yield is 85.1%.
• the extraction yield is 85.7%.
• the extraction yield is 79.2%.
• the cake is then washed with 3 times 2.4 l of water at 40 ° C. and then dried at 50 ° C.
• the cake is then washed with 3 times 2.4 l of water at 40 ° C. and then dried at 50 ° C.
• the cake is then washed with 3 times 2.4 l of water at 40 ° C. and then dried at 50 ° C.
• the rare earths present in the leach liquors obtained according to the invention can then be extracted according to conventional methods, for example
• NPPA sulphate
• TBP / D2EHPA nitric medium

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