CS267903B1 - The way of neutralizing mineral contaminated acids - Google Patents
The way of neutralizing mineral contaminated acids Download PDFInfo
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- CS267903B1 CS267903B1 CS868664A CS866486A CS267903B1 CS 267903 B1 CS267903 B1 CS 267903B1 CS 868664 A CS868664 A CS 868664A CS 866486 A CS866486 A CS 866486A CS 267903 B1 CS267903 B1 CS 267903B1
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Abstract
Rieši sa neutrálizácia minerálnych znečistěných kyselin s alkáliami. Minerálně kyseliny sa zneutralizujú so znečistěným hydroxidom sodným, vyzrážané nečistoty sa oddelia sedimentáciou a reakčná zmes sa doneutralizuje s hydroxidom vápenatým v přítomnosti polyelektrolytu a vyzrážané nečistoty sa oddelia sedimentáciou.The neutralization of contaminated mineral acids with alkalis is addressed. Mineral acids are neutralized with contaminated sodium hydroxide, precipitated impurities are separated by sedimentation, and the reaction mixture is further neutralized with calcium hydroxide in the presence of a polyelectrolyte, and precipitated impurities are separated by sedimentation.
Description
CS 267 903 Q1 1EN 267 903 Q1 1
Vynález rieši spůsob neutralizácie minerálnych kyselin vznikajúcich v chemickompr iemysle. V priemysle vel'ml často odpadávajú znečistěné kyseliny, pričom vzniká problém s ichlikvidáciou. Pri vypúšťaní do vodných tokov sa musia správcovi toku platit’ poplatky zaaciditu. NajčastejSie sa odpadně kyseliny před vypúSťanim do vodných tokov neutralizuji)najma s hydroxidom vápenatým.The invention solves the process of neutralizing mineral acids produced in the chemical industry. In the vel'ml industry, contaminated acids often fall off, causing problems with their disposal. When discharging into watercourses, the flow manager has to pay zaacidity fees. Most often, the acids are neutralized prior to discharging into aqueous streams, especially with calcium hydroxide.
Vyššie uvedené nedostatky sú zmiernené spósobom neutralizácie minerálnych znečistě-ných kyselin, podstata ktorého spočiva v tom, že sa minerálně kyseliny zneutralizujús alkaliami. Minerálně kyseliny sú znečistěné s organickými látkami, predovšetkým s kys-líkatými, sírnyini, dusíkatými, chl órder i vá tmi uhťovodíkov a anorganickými látkami, najmasíranmi, chloridmi a kationmi sodíka, vápnika, horčíka, železa, hliníka, zinku. Minerálněkyseliny sa predncutra 1izujú s hydroxidom sodným obsahujúcim ako nečistoty xantogenátcelulózy, sulfid sodný, polysulfid sodný, síran sodný, tiosíran sodný, siričitan sodný.The aforementioned drawbacks are alleviated by the method of neutralizing mineral contaminated acids, the principle being that the mineral acids are neutralized with alkali. Mineral acids are contaminated with organic substances, especially with acidic, sulfuric, nitrogenous, chlorinated hydrocarbons and inorganic substances, the most disulphurized, chloride and cations of sodium, calcium, magnesium, iron, aluminum, zinc. Mineral acids are pretreated with sodium hydroxide containing xanthogenate cellulose, sodium sulfide, sodium polysulfide, sodium sulfate, sodium thiosulfate, sodium sulfite.
Po predneutralizácii sa vyzrážané nečistoty ako celulóza, síra, sulfid zinočnatý s výho-dou oddělí od reakčnej zmesi sedimentáciou. Reakčná zmes sa potom doneutra 1 izuje s hy-droxidom vápenatým na hodnotu pH 5,5 až 0,5 s výhodou v přítomnosti polyelektrolytu. Vy-zrážané nečistoty, najma hydroxid železitý, horečnatý, hlinitý a zinočnatý sa od reakčnejzmesi oddelia sedimentáciou. Výhodou pódia vynálezu je, že sa minerálně znečistěné kyseliny predneutralizujús odpadnými. alkalickými luhmi, ktoré obsahujú xantogenát celulózy, sulfid sodný, poly-sulfid sodný a iné nečistoty. Pri reakcii sa vyzrážajú nečistoty ako celulóza, sulfid zi-nočnatý, síra, ktoré sa oddelia z reakčnej zmesi sedimentáciou vo formě kalu. Po doneu-tralizovaní s hydroxidom vápenatým nám vo formě kalu vysedimentujú hydroxidy zinočnatý,železitý, hlinitý, horečnatý. Po zneutralizovaní minerálnych kyselin a znečistěného hy-droxidu sodného sa při vypuštění do vodného toku dostane menej znečisťujúcich látok, akokeby sa vypúšťali oddelene, alebo sa vypúšťali po separátnej neutrálizácii. Zinok, ktorýje toxický pre povrchové toky sa odstráni z minerálnych kyselin prakticky všetok. Vypú-šťaním zneutralizovaných odpadových vód sa odstránia poplatky za vypúšťanie kyslých, ale-bo alkalických vod do vodného toku, ktoré sú povinné platit správcovi vodného toku. Přiklad 1After pre-neutralization, the precipitated impurities such as cellulose, sulfur, zinc sulfide are preferably separated from the reaction mixture by sedimentation. The reaction mixture is then carried out with calcium hydroxide to a pH of 5.5 to 0.5, preferably in the presence of a polyelectrolyte. The precipitated impurities, in particular ferric, magnesium, aluminum and zinc hydroxides, are separated from the reaction mixture by sedimentation. An advantage of the invention is that the mineral contaminated acids are pre-neutralized by the waste. alkaline liquors containing cellulose xanthate, sodium sulfide, sodium sulfide and other impurities. In the reaction, impurities such as cellulose, zinc sulfide, sulfur precipitate, which are separated from the reaction mixture by sedimentation in the form of sludge. After being carried out with calcium hydroxide, zinc hydroxides, iron (III), aluminum (II), and magnesium hydroxides are used as sludge. After neutralization of the mineral acids and the contaminated sodium hydroxide, less pollutants are obtained when discharged into the watercourse, if they are discharged separately or discharged after separate neutralization. Zinc, which is toxic to surface streams, is virtually removed from the mineral acids. The discharge of neutralized wastewater removes the charges for discharging the acidic or alkaline waters into the watercourse that are required to pay the watercourse manager. Example 1
Znečistěná minerálna kyselina mala následovně zloženie:Contaminated mineral acid has the following composition:
ChSK GCr, 2 h) 790 mg 0 hodnota pH 1,9 2- SO/ 1 650 mg/1 Cl" 1 125 mg/1 Mg2* 101 mg/1 Pe3 + 18 mg/1 AI3* 14 mg/1 Zn2* 8 mg/1COD GCr, 2 h) 790 mg 0 pH value 1.9 2 SO / 1 650 mg / 1 Cl "1 125 mg / 1 Mg2 * 101 mg / 1 Pe3 + 18 mg / l AI3 * 14 mg / 1 Zn2 * 8 mg / l
Znečistěný hydroxid sodný mal následovně zloženie:Contaminated sodium hydroxide has the following composition:
NaOH xantogenát celulózyNaOH cellulose xanthate
Na2S04Na 2 SO 4
Na2S, ha2Sx ako Na^SNa 2 S, ha 2 S x as Na 2 S
Na2S0jNa2S0j
Na2S20j 21 9/1 0,2 9/1 2,2 g/i 1,9 g/i 0,2 g/i 0,039 9/1Na 2 S 2 O 3 21 9/1 0.2 9/1 2.2 g / i 1.9 g / i 0.2 g / i 0.039 9/1
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS868664A CS267903B1 (en) | 1986-11-26 | 1986-11-26 | The way of neutralizing mineral contaminated acids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS868664A CS267903B1 (en) | 1986-11-26 | 1986-11-26 | The way of neutralizing mineral contaminated acids |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS866486A1 CS866486A1 (en) | 1989-07-12 |
| CS267903B1 true CS267903B1 (en) | 1990-02-12 |
Family
ID=5437512
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS868664A CS267903B1 (en) | 1986-11-26 | 1986-11-26 | The way of neutralizing mineral contaminated acids |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS267903B1 (en) |
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1986
- 1986-11-26 CS CS868664A patent/CS267903B1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CS866486A1 (en) | 1989-07-12 |
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