SK277722B6 - Method of elaboration a liquid waste after processing of potassium salts of benzylpenicillin and phenoxymethylpenicillin - Google Patents
Method of elaboration a liquid waste after processing of potassium salts of benzylpenicillin and phenoxymethylpenicillin Download PDFInfo
- Publication number
- SK277722B6 SK277722B6 SK192490A SK192490A SK277722B6 SK 277722 B6 SK277722 B6 SK 277722B6 SK 192490 A SK192490 A SK 192490A SK 192490 A SK192490 A SK 192490A SK 277722 B6 SK277722 B6 SK 277722B6
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- liquid waste
- acetone
- benzylpenicillin
- phenoxymethylpenicillin
- processing
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Abstract
Description
Podstata spôsobu spracovania kvapalného odpadu po výrobe draselnej soli benzylpenicilínu alebo fenoxymetylpenicilínu spočíva podľa vynálezu v tom, že sa z kvapalného odpadu 40 až 85 % hmotn. kyselinou fosforeč- 45 nou za prítomnosti 20 až 60 % obj. acetónu vyzráža požadovaný dihydrofosforečnan draselný. Po jeho odseparovaní sa upravia získané matečné lúhy kvapalného odpadu kryštalickým hydrogénuhličitanom sodným alebo hydroxidom sodným na hodnotu pH 7 až 9, s výhodou na 50 pH 8. Po ochladení vzniknutého reakčného roztoku na teplotu +2 až -10 ’C sa odseparuje požadovaný kryštalický trihydrát octanu sodného, zo zvyšného kvapalného odpadu sa oddestiluje acetón a konečný kvapalný odpad sa podrobí biologickému čisteniu. 55According to the invention, the process for the treatment of liquid waste after production of the potassium salt of benzylpenicillin or phenoxymethylpenicillin consists of 40 to 85 wt. phosphoric acid in the presence of 20 to 60 vol. of acetone precipitates the desired potassium dihydrophosphate. After separation, the mother liquors obtained are crystallized with crystalline sodium bicarbonate or sodium hydroxide to a pH of 7 to 9, preferably 50 to pH 8. After cooling the resulting reaction solution to +2 to -10 ° C, the desired crystalline acetate trihydrate is separated off Sodium is distilled from the remaining liquid waste and the final liquid waste is subjected to biological treatment. 55
Spôsob podľa vynálezu sa vykonáva tak, že sa z kvapalného odpadu (skladajúceho sa z vodnej fázy a rôznych matečných lúhov) po ukončení vlastnej výroby draselných solí vyzráža kyselinou fosforečnou v prítomnosti acetónu dihydrofosforečnan draselný, ktorý sa odsepa- 60 ruje. Z takto získaných matečných lúhov, ktoré okrem rôznych balastových látok obsahujú značné množstvo kyseliny octovej, sa vyzráža opatrným pridávaním kryštalického hydrogénuhličitanu sodného alebo hydroxidu sodného (tiež kryštalického alebo vo forme koncentro- 65 vaného roztoku) trihydrát octanu sodného, ktorého rozpustnosť sa zníži pridaním acetónu (20 až 50 % obj. acetónu na objem matečných lúhov). Potom sa reakčný roztok ochladí na 0 ’C. Po jednoduchom oddestilovaní acetónu sa konečný kvapalný odpad podrobí biologickému čisteniu a zregenerovaný acetón sa opäť použije. Spôsob podľa vynálezu vylučuje nežiaduce znečistenie odpadových vôd a navyše sa získava v pomerne vysokej čistote dihydrofosforečnan draselný a trihydrát octanu sodného, ktoré majú široké použitie v poľnohospodárstve, v chemickom a papierenskom priemysle.The process according to the invention is carried out by precipitation of liquid waste (consisting of the aqueous phase and various mother liquors) after the end of the production of the potassium salts by phosphoric acid in the presence of acetone, potassium dihydrophosphate, which is separated off. The mother liquors thus obtained, which contain a considerable amount of acetic acid in addition to the various ballast substances, are precipitated by the careful addition of crystalline sodium bicarbonate or sodium hydroxide (also crystalline or in the form of a concentrated solution) sodium acetate trihydrate, whose solubility is reduced by acetone ( 20 to 50% by volume of acetone per volume of mother liquors). Then the reaction solution is cooled to 0 C. C. After simply distilling off the acetone, the final liquid waste is subjected to biological purification and the recovered acetone is reused. The process according to the invention avoids unwanted contamination of the waste water and, moreover, is obtained in relatively high purity potassium dihydrogen phosphate and sodium acetate trihydrate, which are widely used in agriculture, in the chemical and paper industries.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Príklad 1:Example 1:
K 2000 ml vodnej fázy s obsahom 406,01 g rozpustných anorganických látok na liter a chemickou spotrebou kyslíka (CHSK) 404 808 mg/1, ktorá vznikla po zrážaní benzylpenicilínu vodným roztokom octanu draselného, sa po častiach pridalo 879 ml 75 %-nej kyseliny fosforečnej technickej, Čím pH reakčnej zmesi kleslo zo 6,8 na 4,0. K tejto zmesi sa za stáleho miešania pridalo ešte 800 ml acetónu a zmes sa ochladila na 0 ’C. Vykryštalizovaný dihydrofosforečnan draselný sa odfiltroval a na filtri sa premyl 1000 ml acetónu. Matečné lúhy a premývací acetón sa zaliali a pH tejto zmesi sa upravilo za miešania a chladenia hydroxidom sodným na pH 8,0. Upravená zmes sa vychladila na -2 ’C a vykryštalizovaný trihydrát octanu sodného sa odfiltroval. Matečné lúhy sa podrobili destilácii, čim sa zregeneroval použitý acetón. Získalo sa 1414 g dihydrofosforečnanu draselného s 99 %-nou čistotou a 1300 g trihydrátu octanu sodného s 98 %nou čistotou. Matečné lúhy po oddestilovaní a doplnení vodou na pôvodný objem obsahovali 70,04 g/1 rozpustných anorganických látok, čo je 17 % z pôvodnej hodnoty a CHSK bola 133 320 mg/1, čo je 32,9 % z pôvodnej hodnoty.To 2000 ml of the aqueous phase containing 406.01 g of soluble inorganic substances per liter and chemical oxygen demand (COD) 404 808 mg / l formed after precipitation of benzylpenicillin with an aqueous potassium acetate solution, 879 ml of 75% acid was added in portions. The pH of the reaction mixture decreased from 6.8 to 4.0. To this mixture was added 800 mL of acetone while stirring, and the mixture was cooled to 0 C. C. The crystallized potassium dihydrogen phosphate was filtered off and washed with 1000 ml acetone. The mother liquors and washing acetone were quenched and the pH of this mixture was adjusted to pH 8.0 with stirring and cooling with sodium hydroxide. The conditioned mixture was cooled to -2 ° C and the crystallized sodium acetate trihydrate was filtered off. The mother liquors were distilled to recover the acetone used. 1414 g of 99% pure potassium dihydrophosphate and 1300 g of 98% pure sodium acetate trihydrate were obtained. The mother liquors after distillation and make-up with water contained 70.04 g / l of soluble inorganic substances, which is 17% of the original value and COD was 133 320 mg / l, which is 32.9% of the original value.
Príklad 2:Example 2:
K 2000 ml vodnej fázy o obsahom 200,0 g rozp. anorganických látok na liter a chemickou spotrebou kyslíka 205 000 mg/1, ktorá vznikla po zrážaní fonoxymetylpenicilínu vodným roztokom octanu draselného, sa po častiach pridalo 420 ml 75 %-nej kyseliny fosforečnej technickej, čím pH reakčnej zmesi kleslo zo 6,7 na 3,9. K reakčnej zmesi sa pridalo ešte 800 ml acetónu a zmes sa ochladila na 0 ’C. Vykryštalizovaný dihydrofosforečnan draselný sa odfiltroval a na filtri sa premyl 1000 ml acetónu. Matečné lúhy a premývací acetón sa zliali a pH tejto zmesi sa upravilo za chladenia a miešania hydroxidom sodným na pH 8,0. Upravená zmes sa vychladila na -6 ’C a vykryštalizovaný trihydrát octanu sodného sa odfiltroval. Matečné lúhy sa podrobili destilácii, čím sa zregeneroval použitý acetón. Získalo sa 680 g dihydrofosforečnanu draselného s 99 %-nou čistotou a 620 g trihydrátu octanu sodného s 97,5 %-nou čistotou.To 2000 ml of an aqueous phase containing 200.0 g of sol. of inorganic substances per liter and a chemical oxygen demand of 205 000 mg / l formed after precipitation of phonoxymethylpenicillin with aqueous potassium acetate solution, 420 ml of 75% phosphoric acid was added in portions, bringing the pH of the reaction mixture down from 6.7 to 3, 9th 800 mL of acetone was added to the reaction mixture and the mixture was cooled to 0 ° C. The crystallized potassium dihydrogen phosphate was filtered off and washed with 1000 ml acetone. The mother liquors and wash acetone were decanted and the pH of the mixture was adjusted to pH 8.0 with cooling and stirring with sodium hydroxide. The conditioned mixture was cooled to -6 ° C and the crystallized sodium acetate trihydrate was filtered off. The mother liquors were subjected to distillation to regenerate the acetone used. 680 g of potassium dihydrogen phosphate of 99% purity and 620 g of sodium acetate trihydrate of 97.5% purity were obtained.
Priemyselná využiteľnosťIndustrial usability
Spôsob podľa vynálezu podstatne skvalitňuje spracovanie odpadov po výrobe draselných soli benzylpenicilínu a fenoxymetylpenicilinu, pretože sa výrazne zníži solnosť odpadov, umožňuje regeneráciu použitého acetónu a získaný vysokokvalitný dihydrogén fosforečnan draselný a trihydrát octanu sodného má ďalšie využitie v poľnohospodárstve ako aj v chemickom a papierenskom priemysle.The process according to the invention significantly improves the treatment of waste after the production of the benzylpenicillin potassium salt and the phenoxymethylpenicillin, since it significantly reduces the salinity of the waste, allows the regeneration of the acetone used and the high quality potassium dihydrogen phosphate and sodium acetate trihydrate obtained.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS901924A CS192490A2 (en) | 1990-04-18 | 1990-04-18 | Method of water phase and mother liquors treatment during phenoxymethylpenicilin or benzyl penicilin production |
Publications (1)
Publication Number | Publication Date |
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SK277722B6 true SK277722B6 (en) | 1994-08-10 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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SK192490A SK277722B6 (en) | 1990-04-18 | 1990-04-18 | Method of elaboration a liquid waste after processing of potassium salts of benzylpenicillin and phenoxymethylpenicillin |
Country Status (2)
Country | Link |
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CS (1) | CS192490A2 (en) |
SK (1) | SK277722B6 (en) |
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1990
- 1990-04-18 SK SK192490A patent/SK277722B6/en unknown
- 1990-04-18 CS CS901924A patent/CS192490A2/en unknown
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Publication number | Publication date |
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CS192490A2 (en) | 1991-11-12 |
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