SU421203A3 - - Google Patents
Info
- Publication number
- SU421203A3 SU421203A3 SU1677524A SU1677524A SU421203A3 SU 421203 A3 SU421203 A3 SU 421203A3 SU 1677524 A SU1677524 A SU 1677524A SU 1677524 A SU1677524 A SU 1677524A SU 421203 A3 SU421203 A3 SU 421203A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- solution
- phase
- organic
- aqueous
- ammonium
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0488—Flow sheets
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G3/00—Compounds of copper
- C01G3/003—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G49/00—Compounds of iron
- C01G49/0009—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G51/00—Compounds of cobalt
- C01G51/003—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G53/00—Compounds of nickel
- C01G53/003—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C381/00—Compounds containing carbon and sulfur and having functional groups not covered by groups C07C301/00 - C07C337/00
- C07C381/12—Sulfonium compounds
-
- 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
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/26—Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
- C22B3/34—Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds containing sulfur, e.g. sulfonium
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Detergent Compositions (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Description
(54) СПОСОБ ОЧИСТКИ Н И КЕЛЬСОДЕРЖ.А.ЩНХ ВОДНЫХ РАСТВОРОВ ОТ nPHAlECER ЗКСТРЛКИJ: (54) METHOD FOR CLEANING OF N AND KELS CONTAINING AQUEOUS WATER SOLUTIONS FROM nPHAlECER STEELERS
1one
I .ч() относшс област мста,1, )1Х , К ЧаСТПОС: -; 1)Ч СМ-;0I .ch () refers to the region Msta, 1,) 1Х, To CHASTPOS: -; 1) H CM-; 0
11икельс();1срж; ни1. 5t).4iiiiix pa.CTBOpk); от ii)n .CCCl ж и.ч КОС о ii jKCi раКИИсГ.11 nickels (); 1srzh; nor1 5t) .4iiiiix pa.CTBOpk); from ii) n .CCCl g and.h CBS about ii jKCi raKIsG.
IrnicCTC ; способ очистки ни1-;о.чьсо,. U). p.iCTnopoii от 1римесс(1 .кичнис ; экcтpaгe T(}, раст- орсшичм в opгa ичccк() )аств(., с иослсдхчоии pcrciicpaiuioi орга 1ичсской фаз i pci i:i);-: 4:iииеГ ее па стадию Э страк,ии.IrnicCTC; method of cleaning ni-; o.chso ,. U). p.iCTnopoii from 1mess (1 .kichnis; extr. T (}, rassishichm in the order of ()) ast ((., from the pcrciicpaiuioi of the 1st phase) i pci i: i; -: 4: i and herGyu; strak, and.
Особе iПОСТ) ирслложсп1 ого с iособа чаетс в ЮМ, что в ачест зс экс , 1)агч 1О.) laioiiKaiiaT .1)С1)Оии .Particular iPOST) is complexed with a special feature in HUM, which is in the quality of ex, 1) agch 1O.) LaioiiKaiiaT .1) C1) Oii.
Это позвол ет 1о:5ыси ь стеиеиь очитки.This allows 1o: 5s of a hundred of stonecrop.
Предложе1 1 ыГ способ состоит в очистке i) .т,ерЖс11ии. растворов жид -:ос: oi экстрак и еГ с io. оргаппческо (j);i31), содержа и1еГ 1 роизводпое сул, СОД, получае/лое , :i,ejb:;u j)eсПчИиеч СОЛ 1ч- О и1аиов()п кис/КТч, () , на eти;:c Л(i)aттp aлКИ .Т cy.4)(i) OЖПO I рО.ТС а ИТЬ К виде форМуЛЬPropose1 1 The method consists in cleaning i). T, ergss11ii. liquid solutions: os: oi extract and eG with io. orgappno (j); i31), containing iGeG 1 production sul, SOD, get / loe,: i, ejb:; uj) esPchIiECh SOL 1ch- O i1aiov () pys ks / KTch, (), on these;: c L (i) aptK ALKI.T cy.4) (i) OZHPO I ros.
I гI g
99
10ten
0.1 - 0.1 -
ЛЮ; 1С15BJ; 1С15
2020
eo.i;eo.i;
2525
ле 1ал..le 1al ..
R,R,
I I
LH, IR,LH, IR,
о oprabout opr
MiOirMiOir
liMII Il 1 ч 1 I Till и.елсзо люжг; Сп п. щ.лсчело 1 ор1-а ;ичсс| оГ( (Ьазь утел обработки П( рас; исаэом. сс1Д,сржан11 ; ct-MiHC лмо 1 исло . су.1ь(раты пли соль MOia.iia. о6; ада-20 кпцсго бо.юе нь:со нм сро;;.ст1К)л1. мом юохва .Кнтпое /Ko.KVio, )н.ер CO.T н.Г1ка, Агедл пли кпба.;:/ а, в .,ор д1 с убв1ван1-1 соодстпа, Коба.п,: Mo/KCi 6ijri) 3::ioHpoii-: liacnujpoM an:.iva и. , iC.u расл5ором соли 5 циика. а aoc.o.THi:ii мс)кет бььп, звлечсм с и()М()п:ыо ал;лл1ач:1ого раслюра, ;;о.те1)жа1дс)d iiiii..T.a суль(11ат аммонии. ; I р и м е 1) i. а:)пготот.зсни;: lao-iU aa )Bor4) ||ро ;зиодао ч) соли с мьфо| |м, неаольпчМосо ;; аред.южечаом снособс ;;чисткп, зак.лючаетс в .л1аон реакнни ciae.Tib чеплел су..:к)о и родаин.лом аммони в ,HOM paciisope в присутствии органического Пример 3. Оиределеиие сгаб 1Л15и о с т и т и о i. и а и а т а с у л ь ф о и и . ZLTs; этого провод г п тнадцать последовательных40 циклов, включающих каждый экстракцию, регелерадпю и промывку согласие епособу, оппсапдом}- в примере 2. Обрабатываем}, сул,15 реактор, Ciijio/Kcinn) yciponciBoM ;;,iH ne рсмсшизана , liiJMciuaioi 250 мл триалк лс . .; ПМ1МС:И, сульфата и ;и)бав,.1 к)г стсхиомсгричсскос ко/тичес но. j)acc4irraii ioc па , раст/юра роданида аммони i. присхтствии 500 ::; li/unui она. После нерсмсии jjjniiisi н ()Tcra ;BaiiH i н течсмше И) мин нз jJcaKTOfia о1дсл1 по 1пл:()д т водную и оргапнчсскхю фазы и опрсД.м 1Ог с Х1Ср кание ) н i поциаиата « аамсдс.г нз :)тих (раз. Пример 2. Очис хлорндных, сульфатщл jiiiTpaT;n,iX jiacTiiopOB со..-1ен :пке,т , содсржани1х а;баль; мед н lu-iHK в ачествс ос юваых нрнмесе, 11рО15од т в делителы;он :иа)( о)ганичсским раствором, И(.). учеа1|, еогмасно JipHAicpy , ирл со()Т11ои ении объема opiaiiiHaecKon н водиой Фаз. равном 3. ,1алео по;1ученн :о опга 1 1ческ чо () HpcjMijiBaxjT водой нри cooTiioiaeHHH ;;ргаиичсско11 и водион фаз. равном 1. О)ган ;ческ чо регенсрирую; рас вором. содер/каищ-л около 00 г/.т сульфата аммочи и 3 мол.,;л аммиака при фатиьл раствор содержит примерио 92 г/л 1 икел и :5 качестве примесей 7,9 г/л кобальта, 3,9 г/л медп и 3.3 г/л иипка. Операции провод т в делительпо , куда номегцают 500 мл очищаемо-го водного раствора и 500 мл |;аствора ти() еу.твфоии , растворе; iioro в Л11-из(1оутилаието11е с содержанием примерно 0,4 моль гиоцппиата на I л расгвора. Соотношение обьемов органичеекой и водной фаз равно 1. Во врем п того, дес того и п тнадцатого циклов определ ют количество металла в частично очип1еииом водно 1 растворе , а также солержанне сульфонн и рсдапнд-иона , нерешсдньчх в водную фазу.liMII Il 1 h 1 I Till and elszo lyuzg; Cn p.shchelo 1 op1-a; ichss | oG ((uzl utel processing P (races; isaeom. ss1D, srzhan 11; ct-MiHC lmo 1 islo. su.1b (rats or salt of MOia.iia. o6; ada-20 kptssgo.yyu n: with nm av ;;; .st1K) l1. mom yoohwa .Kntopoy /Ko.KVio,) n. er CO.T n.G1ka, Agedl p kpba.;: / a, v., op d1 s ubv1van1-1 soodstpa, Koba.n: Mo / KCi 6ijri) 3 :: ioHpoii-: liacnujpoM an: .iva i., IC.u from the salt of the 5th signal salt and aoc.o.THi: ii ms) ket byp, light s and () M () n: yo al; hl1ach: 1st solution, ;; o.te1) ja1ds) d iiiii..Ta sul (11at ammonium; i p and m 1) i. a:) pgotot.zsni ;: lao-iU aa) Bor4) || ro; zydao h) salts with mofo | | m, neaoltchMoso ;; arezuschomososnos ;; chistkp, zak.lyuyutsya in. liaon reaknni ciae.Tib thrashed soo ..: k) o and ammonium rhodinom in, HOM paciisope in the presence of organic Example 3. about i. and a and a t and with a l l f about and and. ZLTs; of this wire r fifteen consecutive 40 cycles, including each extraction, recovery and washing consent to the method, oppsapd} - in example 2. Process}, sul, 15 reactor, Ciijio / Kcinn) yciponciBoM ;;, iH ne rmsmsizana, liiJMcioioi 250 mL triple . ; PM1MS: I, sulphate and; and) bav, .1 k) g st schhomsgrichskos ko / ticho. j) acc4irraii ioc pa, growth / jurassic ammonium rodanide i. the number 500 ::; li / unui she. After non-jjjniiisi n () Tcra; BaiiH i nsmshimi I) min nz jJcaKTOfia o1dsl1 to 1pl :() d t water and organic phase and opresDm 1Og with H1Srkanie) i of the “adamsdg” Example 2. Allocation of chlorend, sulphate jiiiTpaT; n, iX jiacTiiopOB with ..- 1en: pke, t, sosrzhani1h; bal; honey n lu-iHK as the main yrnmes nrnmes, 11rO15od t to dividers; (o) ganichssky solution, and (.). study1 |, JogHAicpy, compatibility with () T11oi tion volume opiaiiiHaecKon n vody Phases. equal to 3., 1 in 1; 1 arrays: o opga 1 1 cho () Hpcj MijiBaxjT with water at cooTiioiaeHHH ;; rgaiichsko11 and waterion phases. equal to 1. O) gan; chescho cho regensiruyu; the thief a content of about 00 g / .t of ammonium sulfate and 3 mol.,; l of ammonia with fatal solution contains approximately 92 g / l 1 and: 5 as impurities 7.9 g / l of cobalt, 3.9 g / l medp and 3.3 g / l ipka. The operations are carried out in a divider, where 500 ml of the purified aqueous solution and 500 ml of the solution are cleaned () EUtvioia, solution; iioro in Л11-из (1утилаието 11е with a content of about 0.4 mol of hyo-hippol per liter of solution. The ratio of the organic and aqueous phases is 1. During the fifth, tenth and fifteenth cycles, the amount of metal in the partial aqueous solution 1 solution is determined as well as the solnerex sulfonn and rsdapdn-ion, not resolved into the aqueous phase.
Результаты опыта ноь:аз лп X()p()() стабильность тнонианата сульфони в ходе носледовательных циклических обработок, что позвол ет проводит бо.тьпюе число онераниГ без добавлени свежего продукта в органнчеиThe results of the test: lp X () p () () are the stability of the sulfonium tononianate during successive cyclic treatments, which makes it possible to carry out a large number of mobile phones without adding fresh organic matter.
() фазу, н 1-:еиысокнй расход тноцнаната нрн |;енрерь вн;ч процессе o6pa6ivi-KH.() phase, n 1-: the highest consumption of the total output of the nrn |; enrer vn; o process o6pa6ivi-kh.
Пред л; о т н з о б р е т е н н Pre l; about t nz about the reference
Способ очистки 11икельсодержаци1х водных растворов от цримесен экстракцией тиоциано1-;ыл; экcтpaгei:тo i, растворенным в органичеcia )M 1)асiBojMiTe.ie, с носледу1он1ей регеиерацнеГ: органпческоГ) фазы п рециркул цией ее на стадию экстр;;кцпц, о т л н ч а ю щ н и с тем, что, с юлыо повы1пе 1 степени очпстки, в ,чтве экстрагснта 11спо, тиоцианат сул1 фоцн .The method of purification of nickel-containing aqueous solutions from tricyames by the extraction of thiocyanol; extracts: to i, dissolved in organic) M 1) asiBoiMiTe.ie, with the following regiatairen: organpskoe) phase by recycling it to the extras stage ;; ctsts, about t You can increase it to 1 degree or less, and, in addition, 11spo, thiocyanate sul1 focn.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7025258A FR2096865B1 (en) | 1970-07-08 | 1970-07-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
SU421203A3 true SU421203A3 (en) | 1974-03-25 |
Family
ID=9058432
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1677524A SU421203A3 (en) | 1970-07-08 | 1971-07-08 |
Country Status (12)
Country | Link |
---|---|
JP (1) | JPS5110572B1 (en) |
AT (1) | AT314477B (en) |
BE (1) | BE769526A (en) |
CA (1) | CA940305A (en) |
DE (1) | DE2133855C3 (en) |
FR (1) | FR2096865B1 (en) |
GB (1) | GB1314924A (en) |
NL (1) | NL147398B (en) |
NO (1) | NO129753B (en) |
OA (1) | OA03758A (en) |
SU (1) | SU421203A3 (en) |
ZA (1) | ZA714513B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1112460A (en) * | 1977-02-28 | 1981-11-17 | Franklin F. Clark | Solvent extraction process |
-
1970
- 1970-07-08 FR FR7025258A patent/FR2096865B1/fr not_active Expired
-
1971
- 1971-06-29 NO NO02474/71A patent/NO129753B/no unknown
- 1971-07-05 GB GB3150271A patent/GB1314924A/en not_active Expired
- 1971-07-05 BE BE769526A patent/BE769526A/en unknown
- 1971-07-07 DE DE2133855A patent/DE2133855C3/en not_active Expired
- 1971-07-07 OA OA54298A patent/OA03758A/en unknown
- 1971-07-07 CA CA117,608A patent/CA940305A/en not_active Expired
- 1971-07-08 JP JP46050659A patent/JPS5110572B1/ja active Pending
- 1971-07-08 AT AT596971A patent/AT314477B/en not_active IP Right Cessation
- 1971-07-08 NL NL717109463A patent/NL147398B/en unknown
- 1971-07-08 SU SU1677524A patent/SU421203A3/ru active
- 1971-07-08 ZA ZA714513A patent/ZA714513B/en unknown
Also Published As
Publication number | Publication date |
---|---|
GB1314924A (en) | 1973-04-26 |
OA03758A (en) | 1971-12-24 |
NL7109463A (en) | 1972-01-11 |
FR2096865A1 (en) | 1972-03-03 |
CA940305A (en) | 1974-01-22 |
DE2133855C3 (en) | 1974-12-05 |
AT314477B (en) | 1974-04-10 |
DE2133855A1 (en) | 1972-01-13 |
JPS5110572B1 (en) | 1976-04-05 |
FR2096865B1 (en) | 1974-05-24 |
BE769526A (en) | 1972-01-05 |
NL147398B (en) | 1975-10-15 |
NO129753B (en) | 1974-05-20 |
DE2133855B2 (en) | 1974-04-04 |
ZA714513B (en) | 1972-06-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES431120A1 (en) | Cyclic process for re-use of waste water generated during the production of UO{HD 2 | |
GB1484860A (en) | Manufacture of boric acid | |
SU421203A3 (en) | ||
US3008990A (en) | Method of extracting acrylamide from its reaction medium | |
US4346061A (en) | Purification of ammonium tungstate solutions | |
GB1187842A (en) | A Process for Treating Coal Schists. | |
DE1445470A1 (en) | Process for the preparation of heterocyclic organic compounds | |
SU783234A1 (en) | Method of producing titanium hydroxide | |
DE2321196A1 (en) | REMOVAL OF MERCURY FROM SEWATER | |
DE1795129C3 (en) | Process for the preparation of alkali metal salts of α-aminobenzylpenicillin and its epimers | |
CN1062884A (en) | Preparation process for high-content sodium rhodanide | |
US1619666A (en) | Process for the extraction of ammonium-aluminum sulphate from aluminum-sulphate solutions containing ferric compounds | |
DE2145321B2 (en) | PROCESS FOR THE PRODUCTION OF POTASSIUM PEROXYDISULFATE | |
GB1036815A (en) | Method of producing n-methyleneglycinonitrile | |
GB1322119A (en) | Recovery of ammonium sulphate | |
JPS55149134A (en) | Manufacture of high purity ammonium molybdate from aqueous alkali solution containing vanadium and molybdenum | |
GB783628A (en) | Improvements in or relating to recovery of thorium from monazite | |
ES8403975A1 (en) | Method of recovering uranium. | |
US2739962A (en) | Production of crystalline procaine penicillin | |
DE519048C (en) | Process for the production of ammonium sulfate | |
CN1037674C (en) | Method for recovering and treating waste liquid containing acid and copper | |
SU134699A1 (en) | The method of obtaining 1-aminoanthraquinone | |
SU779298A1 (en) | Method of producing ammonium tiosulfate | |
GB596086A (en) | Improved process for the recovery of chemical products from viscose rayon spinning baths | |
Ice | The use of ion exchange resins in the decomposition of lead salts of flavonoid compounds |