PL8745B1 - Method of cleaning chemicals. - Google Patents
Method of cleaning chemicals. Download PDFInfo
- Publication number
- PL8745B1 PL8745B1 PL8745A PL874527A PL8745B1 PL 8745 B1 PL8745 B1 PL 8745B1 PL 8745 A PL8745 A PL 8745A PL 874527 A PL874527 A PL 874527A PL 8745 B1 PL8745 B1 PL 8745B1
- Authority
- PL
- Poland
- Prior art keywords
- silica gel
- chemicals
- solutions
- cleaning chemicals
- solution
- Prior art date
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- 239000000126 substance Substances 0.000 title claims description 8
- 238000000034 method Methods 0.000 title claims description 4
- 238000004140 cleaning Methods 0.000 title 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 229910021538 borax Inorganic materials 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000004328 sodium tetraborate Substances 0.000 description 2
- 235000010339 sodium tetraborate Nutrition 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 125000005342 perphosphate group Chemical group 0.000 description 1
- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical group S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229960001922 sodium perborate Drugs 0.000 description 1
- YKLJGMBLPUQQOI-UHFFFAOYSA-M sodium;oxidooxy(oxo)borane Chemical compound [Na+].[O-]OB=O YKLJGMBLPUQQOI-UHFFFAOYSA-M 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
Chemikalja, uzywane do wyrobu pro¬ duktów zawierajacych czynny tlen, musza byc, jak wiadomo, bardzo czyste. Nawet bardzo nieznaczne zanieczyszczenia, dzia¬ lajac katalitycznie, rozkladaja pewne zwiazki i zmniejszaja uzysk, oraz trwalosc otrzymanych produktów. Chemikalja, o których mowa, musza byc zatem mozliwie czyste i wolne przedewszystkiem od do¬ mieszek dzialajacych katalitycznie. Tak np. przy wyrobie nadboranów i nadwegla¬ nów, zwiazki, uzywane do ich wyrobu, wiec boraks, soda zraca i kalcynowana so¬ da, musza byc mozliwie czyste, zwla¬ szcza gdy wyrób wymienionych produk¬ tów odbywa sie droga elektrolityczna. Po¬ dobnie przy wytwarzaniu wody utlenionej, nadsiarczanów, nadfosforanów, chemikalja dostarczajace tlen musza byc bardzo do¬ kladnie czyszczone, aby nie zawieraly ka¬ talizatorów.W celu oczyszczenia stosuje sie zwykle przekrystalizowywanie. Doswiadczenie wy¬ kazalo jednak, ze uzysk tlenu i trwalosc produktu pogarszaja nawet tak male do¬ mieszki (zanieczyszczen), których istnienia nie mozna praktycznie wykazac. Znaczny wplyw maja juz np. nieznaczne zawarto¬ sci soli ciezkich metali zawartych normal¬ nie w wodzie wodociagowej, a nawet i de¬ stylowanej. Glównie wchodzi tu w rachu¬ be mangan, miedz i niezmiernie male ila¬ sci platyny.Próby wykazaly, ze te nieznaczne do¬ mieszki katalizatorów mozna usuwac dzia¬ lajac na roztwory oczyszczanych zwiazkówzelem krzemionkowym, który ma prawdo¬ podobnie wlasnosc pochlaniania wymienio¬ nych katalizatorów. Tak np. wystarcza je¬ zeli roztwór boraksu lub sody (po wydzie¬ leniu z niego tych ilosci zwiazków ciezkich metali, które dadza sie usunac) wygotuje sie jeszcze raz przed krystalizacja ze sproszkowanym zelem krzemionkowym, W tym wypadku wystarczy np. 2 kg zelu na 1 m3 roztworu. Sól wykrystalizowana z tak przerobionego roztworu i przeprowa¬ dzona w odpowiedni nadzwiazek daje naj¬ wiekszy uzysk, a otrzymany produkt jest bardzo trwaly.Mieszanie roztworów z zelem moze sie takze odbywac na zimno, lecz proces trwa wtedy dluzej. Przeróbka na zimno ma za¬ stosowani wtedy, gdy z roztworów nie wydziela sie wspomnianych chemikaljów, lecz przerabia sie je dalej bezposrednio w postaci roztworów. W ten sposób odbywa sie np, proces wytworzenia nadboranu so¬ dowego przez dodawanie wody utlenionej do roztworu metaloboranu sodowego.Przez zel krzemionkowy rozumie sie grubsza lub drobniejsza mase ziarnista czystego kwasu krzemowego (porównaj np.Meyer Zeitschrift fur angew. Chemie, tom 37, rocznik 1924, str. 36 i 209 i amerykan¬ ski patent Nr 1297 724). Zuzyty zel krze¬ mionkowy moze byc ponownie uzyty po wyplókaniu i regeneracji zapomoca kwasu oraz ogrzewania. PLThe chemicals used in the manufacture of products containing active oxygen must, as is well known, be very pure. Even very slight impurities, acting catalytically, break down certain compounds and reduce the yield and durability of the products obtained. The chemicals in question must therefore be as pure as possible and free, in particular, from catalytically active additives. For example, in the production of perborates and percarbonates, the compounds used in their production, so borax, soda and calcined soda must be as pure as possible, especially when the production of the above-mentioned products is carried out by electrolysis. Likewise, in the production of hydrogen peroxide, persulfates, and perphosphates, the oxygen-supplying chemicals must be very thoroughly cleaned to be free of catalysts. Recrystallization is usually used for purification. However, experience has shown that the oxygen yield and product stability are deteriorated by even such small admixtures (impurities), the existence of which cannot be practically demonstrated. For example, even small amounts of heavy metal salts normally contained in tap water, and even distilled water, have a significant influence. These are mainly manganese, copper and extremely small amounts of platinum. Trials have shown that these slight admixtures of catalysts can be removed by treating the solutions of the compounds to be purified with silica gel, which is likely to absorb the catalysts mentioned. . For example, it is sufficient if the borax or soda solution (after separating from it those quantities of heavy metal compounds which can be removed) is boiled once more before crystallizing with powdered silica gel, in this case, for example, 2 kg of gel per 1 m3 of solution. The salt crystallized from such a processed solution and transformed into an appropriate excipient gives the greatest yield, and the obtained product is very stable. Mixing the solutions with the gel can also take place in the cold, but the process takes longer then. Cold processing is used when the said chemicals are not separated from the solutions, but are further processed directly in the form of solutions. In this way, for example, the preparation of sodium perborate takes place by adding hydrogen peroxide to a sodium metalloborate solution. Silica gel is understood to mean a coarser or finer granular mass of pure silicic acid (see, for example, Meyer Zeitschrift fur angew Chemie, vol. 37, yearbook). 1924, pages 36 and 209 and U.S. Patent No. 1,297,724). The spent silica gel can be reused after washing and regeneration with acid and heating. PL
Claims (2)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL8745B1 true PL8745B1 (en) | 1928-05-31 |
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