NO134704B - - Google Patents
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- Publication number
- NO134704B NO134704B NO3143/73A NO314373A NO134704B NO 134704 B NO134704 B NO 134704B NO 3143/73 A NO3143/73 A NO 3143/73A NO 314373 A NO314373 A NO 314373A NO 134704 B NO134704 B NO 134704B
- Authority
- NO
- Norway
- Prior art keywords
- gold
- solution
- nitric acid
- platinum group
- metals
- Prior art date
Links
- 239000010931 gold Substances 0.000 claims description 30
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 25
- 229910052737 gold Inorganic materials 0.000 claims description 25
- 229910052751 metal Inorganic materials 0.000 claims description 17
- 239000002184 metal Substances 0.000 claims description 17
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 16
- 150000002739 metals Chemical class 0.000 claims description 11
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 10
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 10
- 229910017604 nitric acid Inorganic materials 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 description 9
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 7
- 238000009835 boiling Methods 0.000 description 7
- 239000002244 precipitate Substances 0.000 description 6
- 239000010948 rhodium Substances 0.000 description 5
- 239000000706 filtrate Substances 0.000 description 4
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 3
- 229910000510 noble metal Inorganic materials 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 229910052741 iridium Inorganic materials 0.000 description 2
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229910052703 rhodium Inorganic materials 0.000 description 2
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- AVXURJPOCDRRFD-UHFFFAOYSA-N Hydroxylamine Chemical compound ON AVXURJPOCDRRFD-UHFFFAOYSA-N 0.000 description 1
- 229910017912 NH2OH Inorganic materials 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 125000001309 chloro group Chemical class Cl* 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- VPCDQGACGWYTMC-UHFFFAOYSA-N nitrosyl chloride Chemical class ClN=O VPCDQGACGWYTMC-UHFFFAOYSA-N 0.000 description 1
- -1 platinum group metals Chemical class 0.000 description 1
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
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
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
-
- 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
- C22B11/00—Obtaining noble metals
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Den foreliggende oppfinnelse vedrører en fremgangsmåte til separering av gull fra metaller tilhørende platinagruppen. The present invention relates to a method for separating gold from metals belonging to the platinum group.
Vanligvis forekommer de fem metaller tilhørende platinagruppen, nemlig platina, palladium, iridium, ruthenium og rhodium sammen med gull i naturen, og disse grunnstoffer må separeres fra hverandre og anrikes for å være anvendbare i han-del eller industri. Vanligvis gjennomføres en begynnende separering av disse grunnstoffer i to grupper ved å behandle grunn-blandingen, som vanligvis er en matteutlutingsrest eller sligg, med kongevann, hvorved platina, palladium og gull oppløses, mens iridium, ruthenium og rhodium stort sett blir tilbake i resten fra denne behandling. De to grupper av metaller som oppnås på denne måte underkastes deretter vanligvis lange og kompliserte separasjonsprosesser for å separere og anrike de enkelte metaller. Usually the five metals belonging to the platinum group, namely platinum, palladium, iridium, ruthenium and rhodium, occur together with gold in nature, and these elements must be separated from each other and enriched in order to be usable in metal or industry. Usually, an initial separation of these elements into two groups is carried out by treating the base mixture, which is usually a matte leach residue or slag, with aqua regia, whereby platinum, palladium and gold dissolve, while iridium, ruthenium and rhodium mostly remain in the residue from this treatment. The two groups of metals obtained in this way are then usually subjected to long and complicated separation processes to separate and enrich the individual metals.
Formålet med den foreliggende oppfinnelse er å frembringe en fremgangsmåte for separering av gull fra andre metaller til-hørende platinagruppen, som kan gjennomføres lettvintere i det minste når det som sluttprodukt kreves gull av høy renhet og/ eller gjøre separeringen av metaller tilhørende platinagruppen som er til stede sammen med gull lettvintere. The purpose of the present invention is to produce a method for separating gold from other metals belonging to the platinum group, which can be carried out more easily, at least when gold of high purity is required as the end product and/or to make the separation of metals belonging to the platinum group which is present together with gold lighters.
Fremgangsmåten ifølge oppfinnelsen kjennetegnes ved at en oppløsning som inneholder gull og minst ett metall tilhørende platinagruppen inndampes til tørr tilstand minst én gang, fortrinnsvis to ganger, med salpetersyre, at resten gjenoppløses i salpetersyre og at det til den resulterende oppløsning til-settes hydrogenperoksyd hvoretter oppløsningen kokes for å The method according to the invention is characterized by the fact that a solution containing gold and at least one metal belonging to the platinum group is evaporated to dryness at least once, preferably twice, with nitric acid, that the residue is redissolved in nitric acid and that hydrogen peroxide is added to the resulting solution, after which the solution be boiled to
felle ut og koagulere gullet som metall. precipitate and coagulate the gold as metal.
Inndampning til tørr tilstand med salpetersyre gjennom-føres for å danne nitosokloridkomplekser av de tilstedeværende metaller. Evaporation to dryness with nitric acid is carried out to form nitrosochloride complexes of the metals present.
Vanligvis oppnås konsentrater av metallene tilhørende platinagruppen og gull som en matteutlutingsrest eller en sligg som behandles for å oppnå de ønskete metaller. Generally, concentrates of the metals belonging to the platinum group and gold are obtained as a matte leach residue or a slag which is processed to obtain the desired metals.
I beskrivelsen vil det bli henvist til det medfølgende flyteskjerna. In the description, reference will be made to the supplied floating core.
En oppløsning (1,75 1) av metaller tilhørende platinagruppen i kongevann, som inneholdt 171.210 mg Pt, 74.790 mg Pd, 14.560 mg Au, 200 mg Rh, 25 mg Ru samt 210 mg Ir ble etter inn-damping til tørr tilstand i "Teflon"-skåler og etter brenning av saltene på en varmeplate- i tretti minutter inndampet til tørr tilstand på et trinn 1 med to like store porsjoner kon-sentrert salpetersyre (2 x 0,55 1). A solution (1.75 1) of metals belonging to the platinum group in aqua regia, which contained 171,210 mg Pt, 74,790 mg Pd, 14,560 mg Au, 200 mg Rh, 25 mg Ru and 210 mg Ir was evaporated to dryness in " Teflon" bowls and after burning the salts on a hot plate for thirty minutes evaporated to dryness on a stage 1 with two equal portions of concentrated nitric acid (2 x 0.55 L).
Saltene ble deretter brent igjen i tretti minutter. The salts were then burned again for thirty minutes.
De tørkete salter ble deretter løst ved koking på et trinn 2 med 10 prosentig salpetersyre ( 2 1) for å frembringe en opp-løsning inneholdende 150 g/l edelt metall. Oppløsningen ble deretter tynnet til 100 g/l edelt metall med kaldt vann (21+31). The dried salts were then dissolved by boiling on a stage 2 with 10 per cent nitric acid (2 1) to produce a solution containing 150 g/l precious metal. The solution was then diluted to 100 g/l precious metal with cold water (21+31).
1 ml H202 pr. g edelt metall (300 ml) ble deretter tilsatt og oppløsningen brakt til å koke igjen og fikk koke i tretti 1 ml H202 per g noble metal (300 mL) was then added and the solution brought to the boil again and allowed to boil for thirty
minutter. Oppløsningen ble avkjølt til 55°C og filtrert under vakuum. minutes. The solution was cooled to 55°C and filtered under vacuum.
Utfellingen ble tilført til en gullanrikningssyklus som begynte på et trinn 3. The precipitate was fed into a gold beneficiation cycle which began at a stage 3.
Utfellingen som ble oppnådd ved utøvelse av den foreliggende oppfinnelse hadde følgende bestanddeler: 50 mg Pt, 10 mg Pd, 13.750 mg Au, 40 mg Rh og spor av Ru. The precipitate obtained by practicing the present invention had the following constituents: 50 mg Pt, 10 mg Pd, 13,750 mg Au, 40 mg Rh and traces of Ru.
Dette urene gull ble oppløst i kongevann (0,06 1) på et trinn 3. Oppløsningen ble inndampet til tørr tilstand, og saltene ble kokt på et trinn 4 med NH^OH (0,06 1) for å løse even-tuelt sølvklorid. Oppløsningen ble avkjølt til 55°C og filtrert. Filtratet som inneholdte bare spor av sølv, ble fjernet. This impure gold was dissolved in aqua regia (0.06 L) in a step 3. The solution was evaporated to dryness and the salts were boiled in a step 4 with NH₂OH (0.06 L) to dissolve any silver chloride . The solution was cooled to 55°C and filtered. The filtrate containing only traces of silver was removed.
Resten ble oppløst i kokende 5 prosentig HNO^ (0,06 1) på et trinn 5. Den uløselige rest ble avfiltrert og villei praksis ha blitt resirkulert til et egnet trinn. The residue was dissolved in boiling 5 percent HNO 2 (0.06 L) on a step 5. The insoluble residue was filtered off and in practice would have been recycled to a suitable step.
Filtratet ble deretter føtt over en kationisk harpiks "Dowex" 50 x 8 på et trinn 6, og'harpiksen holdt tilbake uedle-metaller, og gull ble vasket gjennom med vann. The filtrate was then passed over a cationic resin "Dowex" 50 x 8 on a stage 6 and the resin retained base metals and gold was washed through with water.
H2°2 ^#03 1) ble tilsatt til den utstrømmende væske på H2°2 ^#03 1) was added to the flowing liquid on
et trinn 7 og kokt i tretti minutter for å felle -ut gullet. Etter avkjøling til 55 C ble oppløsningen\filtrert. a step 7 and boiled for thirty minutes to precipitate -out the gold. After cooling to 55°C, the solution was filtered.
x x
Den tørkete utfelling var det endelige gull som hadde en renhet på mer enn 99,9%. The dried precipitate was the final gold that had a purity of more than 99.9%.
Det totale utbyttet var Au = 9000 mg som er omtrent 60% The total yield was Au = 9000 mg which is about 60%
av det opprinnelige gullinnhold på 14.560 mg Au. of the original gold content of 14,560 mg Au.
Gullet i filtratet ble utfelt ved å koke oppløsningen The gold in the filtrate was precipitated by boiling the solution
med maursyre (12 ml) på et trinn 8 og ved å regulere løsning-ens pH til 5,0 med Na2C03 (10 g). Oppløsningen ble avkjølt og filtrert. Filtratet ble fjernet og inneholdt ingen edle metaller. with formic acid (12 ml) on a step 8 and by adjusting the pH of the solution to 5.0 with Na 2 CO 3 (10 g). The solution was cooled and filtered. The filtrate was removed and contained no noble metals.
Ved fremgangsmåten ifølge oppfinnelsen ble det i forhold til kjent teknikk således lettvint og effektivt oppnådd gull med høy renhet. Dette fremgår av følgende sammenligningsforsøk. With the method according to the invention, gold with high purity was thus easily and effectively obtained compared to known techniques. This is evident from the following comparison test.
Tre oppløsninger av klorkomplekser av metaller tilhørende platinagruppen og gull ble inndampet til tørr tilstand i en "Teflon"-skål. De derved oppnådde salter ble brent i tretti minutter på en varmeplate hvis temperatur var 130°C. Three solutions of chlorine complexes of platinum group metals and gold were evaporated to dryness in a "Teflon" dish. The salts thus obtained were burned for thirty minutes on a hot plate whose temperature was 130°C.
Innholdet av edle metaller i hver av de opprinnelige opp-løsninger var: 17.121 mg Pt, 7.479 mg Pd, 1.456 mg Au, 200 mg Rh, 25 mg Ru og 210 mg Ir. The content of noble metals in each of the original solutions was: 17,121 mg Pt, 7,479 mg Pd, 1,456 mg Au, 200 mg Rh, 25 mg Ru and 210 mg Ir.
De tørre salter ble behandlet på forskjellige måter: The dry salts were treated in different ways:
a) Saltene ble oppløst i 250 ml kokende vann hvoretter det ble tilsatt 25 ml (100 vol) hydrogenperoksyd, og kokingen ble fortsatt i 30 minutter. Oppløsningen ble avkjølt til 55°C og den oppnådde utfelling avfiltrert. b) De tørre salter ble inndampet til tørr tilstand med 25 ml 55 prosentig salpetersyre, og deretter oppløst i 2 50 ral 5 prosentig salpetersyre under koking. Deretter ble det tilsatt 25 ml (100 vol) hydrogenperoksyd, og kokingen ble fortsatt i tretti minutter. Oppløsningen ble avkjølt til 55°C og den oppnådde ufelling avfiltrert. c) De tørre salter ble behandlet som under b), men inn-damping med 55 prosentig salpetersyre ble fortsatt med to 25 ml a) The salts were dissolved in 250 ml of boiling water after which 25 ml (100 vol) of hydrogen peroxide was added, and the boiling was continued for 30 minutes. The solution was cooled to 55°C and the resulting precipitate was filtered off. b) The dry salts were evaporated to dryness with 25 ml of 55 percent nitric acid, and then dissolved in 2 50 ral of 5 percent nitric acid while boiling. Then 25 ml (100 vol) of hydrogen peroxide was added and boiling was continued for thirty minutes. The solution was cooled to 55°C and the precipitate obtained was filtered off. c) The dry salts were treated as under b), but evaporation with 55 percent nitric acid was continued with two 25 ml
porsjoner. portions.
"Utvinningen av gull økte altså fra 25,8% ifølge a) til ■87,5%: ifølge b) og 95,3% ifølge c). Renheten til gullet ifølge c) var så høy som 91,6%, oppnådd fra en oppløsning hvis gull-gehalt var bare 5,5%..■ "The extraction of gold thus increased from 25.8% according to a) to ■87.5%: according to b) and 95.3% according to c). The purity of the gold according to c) was as high as 91.6%, obtained from a solution whose gold content was only 5.5%..■
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ZA725488A ZA725488B (en) | 1972-08-10 | 1972-08-10 | Improvements in or relating to the separation and purification of gold |
Publications (2)
Publication Number | Publication Date |
---|---|
NO134704B true NO134704B (en) | 1976-08-23 |
NO134704C NO134704C (en) | 1976-12-01 |
Family
ID=25565244
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO733143A NO134704C (en) | 1972-08-10 | 1973-08-07 |
Country Status (9)
Country | Link |
---|---|
JP (1) | JPS5234246B2 (en) |
BE (1) | BE803391A (en) |
CA (1) | CA998533A (en) |
FI (1) | FI58161C (en) |
FR (1) | FR2195690B1 (en) |
GB (1) | GB1434288A (en) |
IT (1) | IT1006037B (en) |
NO (1) | NO134704C (en) |
ZA (1) | ZA725488B (en) |
-
1972
- 1972-08-10 ZA ZA725488A patent/ZA725488B/en unknown
-
1973
- 1973-07-27 FI FI2370/73A patent/FI58161C/en active
- 1973-07-27 GB GB3594473A patent/GB1434288A/en not_active Expired
- 1973-07-31 CA CA177,788A patent/CA998533A/en not_active Expired
- 1973-08-07 NO NO733143A patent/NO134704C/no unknown
- 1973-08-09 IT IT27710/73A patent/IT1006037B/en active
- 1973-08-09 BE BE134383A patent/BE803391A/en unknown
- 1973-08-10 JP JP7389376A patent/JPS5234246B2/ja not_active Expired
- 1973-08-10 FR FR7329341A patent/FR2195690B1/fr not_active Expired
Also Published As
Publication number | Publication date |
---|---|
GB1434288A (en) | 1976-05-05 |
ZA725488B (en) | 1973-09-26 |
CA998533A (en) | 1976-10-19 |
JPS5234246B2 (en) | 1977-09-02 |
FR2195690A1 (en) | 1974-03-08 |
FI58161C (en) | 1980-12-10 |
JPS4945823A (en) | 1974-05-01 |
FI58161B (en) | 1980-08-29 |
AU5881173A (en) | 1974-10-10 |
BE803391A (en) | 1973-12-03 |
IT1006037B (en) | 1976-09-30 |
DE2340157A1 (en) | 1974-02-28 |
DE2340157B2 (en) | 1975-10-23 |
FR2195690B1 (en) | 1976-11-19 |
NO134704C (en) | 1976-12-01 |
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