SK13996A3 - Treatment method of waste water containing soluble phosphates by flocculation process - Google Patents
Treatment method of waste water containing soluble phosphates by flocculation process Download PDFInfo
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- SK13996A3 SK13996A3 SK13996A SK13996A SK13996A3 SK 13996 A3 SK13996 A3 SK 13996A3 SK 13996 A SK13996 A SK 13996A SK 13996 A SK13996 A SK 13996A SK 13996 A3 SK13996 A3 SK 13996A3
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- waste water
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
Spôsob čistenia odpadovej vody s obsahom rozpustných fosforečnanov zrážacim postupom.Process for the purification of waste water containing soluble phosphates by a precipitation process.
Oblasť technikyTechnical field
Vynález sa týka spôsobu čistenia odpadovej vody silne znečistenej fosforečnanmi v rôzných iontových formách zrážacim postupom.The invention relates to a process for the purification of waste water heavily contaminated with phosphates in various ionic forms by a precipitation process.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Odpadové vody z chemického priemyslu, obsahujúce rozpustné formy fosforečnanov, majú obvykle hodnotu pH v oblasti slabo kyslej až slabo zásaditej. V tejto oblasti pH sú fosforečnany prítomné prevažne vo forme dihydrogenfosforečnanov a monohydrogenfosforečnanov. Pri čistení týchto vôd sa obvykle používa zrážacích postupov, pri ktorých sa využíva nízka rozpustnosť niektorých fosforečnanov, napr. železa alebo vápnika. V prípade zrážania fosforečnanov železa je potrebný prebytok zrážacieho činidla v dôsledku inaktivacie časti činidla ’nydrolýzou a výsledný produkt má pre prítomnosť železa sťažené ďalšie využitie.Waste waters from the chemical industry, containing soluble forms of phosphates, usually have a pH in the region of weakly acidic to weakly basic. In this pH range, phosphates are predominantly present in the form of dihydrogen phosphates and monohydrogen phosphates. In the purification of these waters, precipitation processes are generally used which utilize the low solubility of some phosphates, e.g. iron or calcium. In the case of the precipitation of iron phosphates, an excess of precipitant is required as a result of the inactivation of a portion of the reagent by hydrolysis, and the resulting product is more difficult to utilize for the presence of iron.
V prípade zrážania fosforečnanu vápenatého sa obvykle používa ako zrážacie činidlo hydroxyd vápenatý. Avšak hydroxid vápenatý sa po prídavku uplatňuje oboma zložkami, a OH”. Ak sa pridá potrebné množstvo iontov málo rozpustného fosfátu vápenatého, sú odpovedajúce ionty OH' v nadbytku, preto zrážanie prebieha v silnej alkalickej oblasti, v ktorej je rozpúšťanie hydroxidu vápenatého obtiažnejšie, čo sa prejavuje záporne v celej postupu. vylúčená zrazenina je ktorý má zloženie Ca5 (P04) 3. (OH) s to iontami Ca2+ i Ca2+ k vylúčeniu technológii zrážacieho prevážne hydroxylapatit, malým podielom monohydrogenfosforečnana vápenatého ( CaHPO4 ) s podielom zložiek Ca : P04 =1,6 : 1. Po odlúčení zrazeniny od vyčistenej vody je potom nutné pred vypustením do odtoku upravovať hodnotu pH prídavkom kyseliny a nežiaducim spôsobomIn the case of calcium phosphate precipitation, calcium hydroxide is usually used as a precipitation agent. However, calcium hydroxide is added by both components, and OH ”. When the required amount of ions of sparingly soluble calcium phosphate is added, the corresponding OH 'ions are in excess, therefore precipitation occurs in a strong alkaline region, in which the dissolution of calcium hydroxide is more difficult, which is shown negatively throughout the process. the precipitate formed is of the composition Ca 5 (PO 4 ) 3 . (OH) with both Ca 2+ and Ca 2+ ions to eliminate the precipitation technology, predominantly hydroxylapatite, with a small proportion of calcium monohydrogen phosphate (CaHPO 4 ) with a proportion of Ca: PO 4 = 1.6: 1. After separation of the precipitate from purified water, it is necessary to adjust the pH by adding acid and undesirable before discharging into the effluent
- 2 tak zvyšovať obsah rozpustených solí. Okrem toho prebieha rozpúšťanie hydroxidu vápenatého v alkalickej oblasti obtiažnejšie, čo sa prejaví záporne v celej technológií zrážacieho postupu.Thus increasing the dissolved salt content. In addition, the dissolution of calcium hydroxide in the alkaline region is more difficult, which is reflected in the entire precipitation process.
Podstata vynálezuSUMMARY OF THE INVENTION
Teraz bolo zistené, že pri čistení odpadných vôd s obsahom rozpustných fosforečnanov zrážacim postupom s využitím nízkej rozpustnosti zlúčenín fosforečnanov s vápenatými iontami, je možné s výhodou postupovať podľa predmetného vynálezu, ktorého podstata spočíva v tom, že sa do čistenej vody pridá hydroxid vápenatý vo vodnej suspenzie alebo v roztoku k úprave pH v reakčnej zmesi v medziach 9,9 až 10,5 a roztok chloridu vápenatého v takom množstve, aby vo výslednej reakčnej zmesi molárný pomer zložiek Ca : PO, bol 1,1 až 1,4 ku 1. Reakčná zmes sa zamieša. Vylúčená zrazenina sa oddelí od vodnej fáze. S výhodou sa pred ukončením miešania pridá do reakčnej zmesi roztok polymerného organického flokulantu, na príklad látky na bázi polyakrylamidu.It has now been found that for the purification of waste waters containing soluble phosphates by a precipitation process using low solubility of calcium phosphate compounds, the present invention is advantageous in that calcium hydroxide in water is added to the purified water. of a suspension or solution to adjust the pH in the reaction mixture within the range of 9.9 to 10.5 and a solution of calcium chloride in an amount such that the molar ratio of Ca: PO components in the resulting reaction mixture is 1.1 to 1.4 to 1. The reaction mixture is stirred. The precipitate formed is separated from the aqueous phase. Preferably, a solution of polymeric organic flocculant, for example a polyacrylamide-based substance, is added to the reaction mixture before the mixing is complete.
Uvedený spôsob prináša rad výhod voči súčasnému stavu. Zrážacia reakcia prebieha okamžite, lebo nie je brzdená sprievodnými pochodmi. Ionty vápnika, vstupujú do reakcie, sú v stechiometrickom zastúpení v tvoriacej sa zrazenine, preto nie je potrebné použitie prebytku činidla. Úprava pH vo vyčistenej vode pred vypustením nevyžaduje veľké dávky kyseliny. Pridanie polymerného organického flokulantu vo vhodnom okamžiku potom spôsobí vytvorenie väčších dobre sedimentujúcich částic.This method brings a number of advantages over the current state. The precipitation reaction proceeds immediately because it is not inhibited by the accompanying processes. The calcium ions entering the reaction are stoichiometric in the precipitate being formed, so there is no need for excess reagent. Adjusting the pH in purified water before discharge does not require large amounts of acid. The addition of the polymeric organic flocculant at the appropriate time then causes the formation of larger, well-settling particles.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Priklad 1.Example 1.
Odpadová voda obsahujúca 6,4 mmol/1 PO, a 0,87 mmol/1Waste water containing 6.4 mmol / l PO and 0.87 mmol / l
Ca2+ pri pH 4,35. Do jedného litra tejto vody sa pridá 8,2 mmol/1 Ca(OH)2 vo vodnej suspenzie. Zmes nadobudla hodnotu pH 10,47. Ďalej je do zmesi pridaný CaCl2 v roztoku v množstve 1,4 mmol/1. Po premiešaní bola zmes ponechaná 30 minút sedimentovať a potom bola vykonaná analýza, ktorej výsledky sú v nižšie uvedenej tabuľke:Ca 2+ at pH 4.35. To one liter of this water was added 8.2 mmol / l Ca (OH) 2 in an aqueous suspension. The mixture reached a pH of 10.47. CaCl 2 in a solution of 1.4 mmol / l is added to the mixture. After stirring, the mixture was allowed to settle for 30 minutes and then analyzed, the results of which are shown in the table below:
Príklad 2.Example 2.
Zrážanie ako v príklade 1 s tým, že jednu minútu pred ukončením miešania sa pridá pomocný flokulant polyakrylamidového typu v množstve 2 mg/1. Výsledný objem kalu po 30 minútovej sedimentácií bol 21 %.Precipitation as in Example 1 except that one minute before the end of stirring, a polyacrylamide-type auxiliary flocculant is added in an amount of 2 mg / L. The resulting sludge volume after 30 min sedimentation was 21%.
Príklad 3.Example 3.
Do jedného litra odpadnej vody z príkladu 1 bolo pridané 7,3 nmol/1 Ca(OH)2 vo vodnej suspenzii. Hodnota pH zmesi bola 10,05. Ďalej bolo pridané CaCl2 v roztoku v množstve 2,3 mmol/1. Po premiešaní bola zmes ponechána 30 minút sedimentovať. Odsadená voda mala pH 9,78, obsahovala 9,3 mg/1 P04 a objem kalubol 36 %.To one liter of the waste water of Example 1 was added 7.3 nmol / L Ca (OH) 2 in an aqueous suspension. The pH of the mixture was 10.05. CaCl 2 in solution was added in an amount of 2.3 mmol / l. After stirring, the mixture was allowed to sediment for 30 minutes. The effluent had a pH of 9.78, contained 9.3 mg / L PO 4 and a calubel volume of 36%.
Priemyselná využitelnosťIndustrial Applicability
Vynález má uplatnenie pri čistení odpadových vôd z chemického priemyslu, ktoré obsahujú rozpustné formy fosforečnanov.The invention has application in the purification of waste water from the chemical industry containing soluble forms of phosphates.
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CZ953387A CZ282683B6 (en) | 1995-12-20 | 1995-12-20 | process of treating waste water containing soluble phosphates by precipitation |
Publications (1)
Publication Number | Publication Date |
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SK13996A3 true SK13996A3 (en) | 1997-07-09 |
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ID=5466656
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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SK13996A SK13996A3 (en) | 1995-12-20 | 1996-01-31 | Treatment method of waste water containing soluble phosphates by flocculation process |
Country Status (2)
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CZ (1) | CZ282683B6 (en) |
SK (1) | SK13996A3 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105502730B (en) * | 2015-11-30 | 2018-06-05 | 湖北宜化集团有限责任公司 | A kind of mixed type chemical fertilizer production waste water physicochemical processing method |
-
1995
- 1995-12-20 CZ CZ953387A patent/CZ282683B6/en not_active IP Right Cessation
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1996
- 1996-01-31 SK SK13996A patent/SK13996A3/en unknown
Also Published As
Publication number | Publication date |
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CZ338795A3 (en) | 1997-07-16 |
CZ282683B6 (en) | 1997-08-13 |
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