CS253906B1 - Isolation method of the palladium from solutions in production and regeneration palladium catalysts - Google Patents
Isolation method of the palladium from solutions in production and regeneration palladium catalysts Download PDFInfo
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- CS253906B1 CS253906B1 CS853092A CS309285A CS253906B1 CS 253906 B1 CS253906 B1 CS 253906B1 CS 853092 A CS853092 A CS 853092A CS 309285 A CS309285 A CS 309285A CS 253906 B1 CS253906 B1 CS 253906B1
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- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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Abstract
Riešenie sa týká sposobu izolácie paládia z roztokov vznikajúiich pri výrobě a regenerácii paládiových katalyzátorov, pričom paládium sa kontinuálně vyzráža vodorozpustnou sofou 2-merkaptobenztiazolu a vzniknutá zrazenina sa následné separuje známými spósobmi.The solution relates to a method of isolating palladium from solutions resulting from production and regeneration palladium catalysts; the palladium is precipitated continuously water-soluble 2-mercaptobenzothiazole salt a the resulting precipitate is subsequently separated known methods.
Description
Vynález sa týká sposobu izolácie paládia z roztokov vznikajúcich pri výrobě a regenerácii paládiových katalyzátorov, obsahujúcich uvedený drahý kov, kontinuálnym vyzrážaním paládia vodorozpustnou solouThe invention relates to a process for the isolation of palladium from solutions resulting from the production and regeneration of palladium catalysts containing said precious metal by the continuous precipitation of palladium with a water-soluble salt
2-merkaptobenztiazolu a následnou separáciou vzniknutej zrazeniny známými sposobmi.2-mercaptobenzothiazole followed by separation of the resulting precipitate by known methods.
Pri manipulácii s roztokmi obsahujúcimi paládium vo velmi nízkej koncentrácii, ktoré vznikajú pri výrobě a regenerácii paládiového katalyzátora, resp. pri spracovaní odpadových vod z procesov regenerácie, je potřebné paládium izolovat a vrátit spát do procesu. Uvedené zriedené Pd roztoky majú často charakter odpadov, pričom obsah drahého kovu neumožňuje ich llkvidáclu, resp. robí ju mimoriadne nákladnou. V případe váčšieho množstva takto znečistěných roztokov je potom výběr vhodnej metódy na izoláciu drahého kovu velmi problematický.When handling palladium-containing solutions at a very low concentration, which arise in the production and regeneration of the palladium catalyst, respectively. In the treatment of wastewater from regeneration processes, it is necessary to isolate the palladium and return it to the process. Said dilute Pd solutions often have the character of wastes, the precious metal content of which does not allow them to be used as a waste metal. makes it extremely expensive. In the case of large amounts of soiled solutions, the choice of a suitable method for the isolation of the precious metal is very difficult.
Doterajšie pokusy izolovania paládia do formy vhodnej pre jeho ďalšie spracovanie a regeneráciu sú založené na primárnom převedení odpadových roztokov obsahujúcich paládium na chloridové roztoky, alebo na převedení paládia do roztokov kyselin. Bolí tiež robené pokusy izolácie paládia z odpadových vod chemisorpciou.Previous attempts to isolate palladium into a form suitable for further processing and recovery are based on the primary conversion of palladium-containing waste solutions into chloride solutions, or on the conversion of palladium into acid solutions. Attempts have also been made to isolate palladium from wastewater by chemisorption.
Nevýhodou uvedených riešení je to, že přítomné nečistoty, najmá tuhé částice a úlety komplikujú, resp. znemožňujú ich aplikáciu.A disadvantage of these solutions is that the impurities, particulate matter and particulate matter present are complicated, respectively. prevent their application.
Převedeme paládia na chloridový roztok vyžaduje ešte ďalšie spracovanie, obdobné ako jeho prevedenie do kyselin. To znamená, že ich priama aplikácia nie je možná. Pri chemisorpcii sa kladů vysoké nároky na příslušný sorbent, ktorý sa ničí vplyvom přítomných komponentov, najmá tuhých častíc a doležitá je i jeho cena. Ďalšie problémy vznikajú s vytěsňováním zakotvenej fázy, resp. s dalším spracovaním eluátov.Converting palladium to a chloride solution requires further processing, similar to converting it into acids. This means that their direct application is not possible. In chemisorption, high demands are placed on the respective sorbent, which is destroyed by the presence of the components present, especially the particulate matter and its cost is also important. Further problems arise with displacement of the anchored phase, respectively. with further processing of the eluates.
Pri zrážadlách je problém s ich selektivitou.In the case of precipitants, there is a problem with their selectivity.
Teraz sa zistilo, že uvedené nedostatky odstraňuje sposob izolácie paládia z odpadových vod podlá vynálezu, ktorého podstata spočívá v tom, že paládium sa kontinuálně vyzráža vodorozpustnou sofou 2-merkaptobenztiazolu pri pH menšom ako 2,5 a vzniknutá zrazenina sa následné separuje známými spSsobmi. Na separáciu je výhodné použit flotáciu kombinovaná s filtráciou, resp. odstredovaním flotačnej pěny. Po odfiltrovaní sa filtračný koláč (paládlová pěna] spálima paládiový koncentrát.It has now been found that the above-mentioned deficiencies are overcome by the process for the isolation of palladium from wastewater according to the invention, characterized in that palladium is continuously precipitated with a water-soluble salt of 2-mercaptobenzothiazole at pH less than 2.5 and subsequently precipitated. For separation it is advantageous to use flotation combined with filtration, respectively. by centrifugation of the flotation foam. After filtration, the filter cake (palladium foam) is burned with palladium concentrate.
Podstata vynálezu spočívá v tom, že celý proces alebo jeho časť sa uskutočňuje kontinuálně.The essence of the invention is that all or part of the process is carried out continuously.
Výhodou uvedeného sposobu izolácie paládia je najmá použitie flotácie, ktorá umožňuje znížiť nároky na filtračně operácie, lebo stačí filtrovat iba vyflotovanú paládiovú pěnu. Uvedený postup je výhodný najmá pri velkých objemoch kvapalín a kontinuálnom vedení procesu.Advantage of said method of palladium insulation is the use of flotation in particular, which makes it possible to reduce the demands on filtration operations, since it is sufficient to filter only the faded palladium foam. This process is particularly advantageous for large volumes of liquids and continuous process guidance.
Nasledujúce příklady osvetlujú, ale neobmedzujú predmet vynálezu.The following examples illustrate but do not limit the scope of the invention.
Příklad 1Example 1
Roztok z regenerácie paládia so zvyškovým obsahom Pd 29,1 mg/kg odpadovej vody, s obsahom železa 150 mg/kg odpadovej vody s hodnotou pH = las prietokom 0,2 kilogramov/min sa zrážal kontinuálně amónnou sofou 2-merkaptobenztiazolu s koncentráciou 8,7 °/o hmotnosti s peničom o obsahu 2 % hmotnosti. Prietok zrážadla bol 25 g za minútu. Po flotácii klesla koncentrácia paládia vo vodě na 0,45 mg/kg, čo představuje výťažok 98,45 °/o. V paládiovej pene bol zistený obsah železa v množstve 10“3 percenta hmotnosti. Na flotáciu sa použil dvojkomorový flotátor s objemom komory 12 1.A palladium recovery solution with a residual Pd content of 29.1 mg / kg wastewater, with an iron content of 150 mg / kg wastewater having a pH = las of 0.2 kilograms / min, was precipitated continuously with ammonium salt of 2-mercaptobenzothiazole at a concentration of 8, 7% by weight with a foam of 2% by weight. The flow rate of the precipitant was 25 g per minute. After flotation, the palladium concentration in water dropped to 0.45 mg / kg, representing a yield of 98.45%. The palladium foam was found iron content of at least 10 "3 percent by weight. A two-chamber flotator with a chamber volume of 12 L was used for flotation.
Příklad 2Example 2
V diskontinuálnom usporiadaní sa k 300 centimetrového3 roztoku elektrolytu z regenerácie Pd s obsahom Pd 9,15 mg/1 a hodnotu pH = 1 přidalo' 1,6 cm3 roztoku amónnej soli 2-merkaptobenztiazolu s koncentráciou 6,5 %. Suspenzia sa po 15 min sfiltrovala cez fritu 84. Vo filtráte bola koncentrácia Pd pod medzou stanovenia analytickej metódy, t. j. 0,1 mg Pd/1. To představuje výťažok 98,9 °/o.In a discontinuous arrangement, 1.6 cm 3 of 6.5% ammonium salt of 2-mercaptobenzothiazole ammonium salt was added to a 300 cm 3 electrolyte solution from Pd regeneration with a Pd content of 9.15 mg / L and a pH = 1. The suspension was filtered through a frit 84 after 15 min. In the filtrate, the Pd concentration was below the assay limit of 0.1 mg Pd / L. This represents a yield of 98.9%.
Příklad 3Example 3
Roztok z regenerácie paládia s obsahom Pd 73,19 mg/kg odpadovej vody s hodnotou pH = 2, s prietokom 240 l/h kontinuálně zrážal sa amónnou sofou 2-merkaptobenztiazolu s koncentráciou 7 % hmotnosti, s peničom o obsahu 1,56 %. Prietok zrážadla bol 9,32 l/h. Po flotácii a flltrécii klesla koncentrácia Pd vo vodě na 0,62 mg/kg, čo představuje výťažok 99,2 %.A palladium recovery solution with a Pd content of 73.19 mg / kg wastewater at pH = 2, with a flow rate of 240 l / h, was continuously precipitated with ammonium salt of 2% mercaptobenzothiazole at a concentration of 1.56%. The precipitation flow rate was 9.32 l / h. After flotation and filtration, the concentration of Pd in water dropped to 0.62 mg / kg, representing a yield of 99.2%.
Ako flotátor bol použitý štvorkomorový flotátor s objemom komory 120 1, na filtráciu vyflotovanej pěny kalolis.A four-chamber flotator with a chamber volume of 120 liters was used as a flotator to filter the floated filter press foam.
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CS853092A CS253906B1 (en) | 1985-04-29 | 1985-04-29 | Isolation method of the palladium from solutions in production and regeneration palladium catalysts |
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CS853092A CS253906B1 (en) | 1985-04-29 | 1985-04-29 | Isolation method of the palladium from solutions in production and regeneration palladium catalysts |
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CS309285A1 CS309285A1 (en) | 1985-08-15 |
CS253906B1 true CS253906B1 (en) | 1987-12-17 |
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