CS231375B1 - The method of pre-treatment of wastewater from the production of urea-formaldehyde adhesives - Google Patents

The method of pre-treatment of wastewater from the production of urea-formaldehyde adhesives Download PDF

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CS231375B1
CS231375B1 CS829706A CS970682A CS231375B1 CS 231375 B1 CS231375 B1 CS 231375B1 CS 829706 A CS829706 A CS 829706A CS 970682 A CS970682 A CS 970682A CS 231375 B1 CS231375 B1 CS 231375B1
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Czechoslovakia
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urea
formaldehyde
production
wastewater
adhesives
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CS829706A
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Czech (cs)
Slovak (sk)
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CS970682A1 (en
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Viktor Berezny
Radislav Lipka
Milan Lichvar
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Viktor Berezny
Radislav Lipka
Milan Lichvar
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Priority to CS829706A priority Critical patent/CS231375B1/en
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Publication of CS231375B1 publication Critical patent/CS231375B1/en

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Abstract

Účelom vynálezu je odstránenie málo stabilného močovino-formaldehydového kondenzátu z odpadových vod z výroby močovi- no-formaldehydových lepidiel a tým vylú- čenie možnosti zanášania potrubí dopravných trás a čistiarenských zariadení. Uvedeného účelu sa dosiahne úpravou odpadových vod z výroby močovino-formaldehy- dových lepidiel anorganickou, alebo organickou kyselinou na pH 1-5, s výhodou na pH 1,2-2. Vypadnutý močovino-formalde- hydový kondenzát sa odseparuje, s výhodou filtráciou alebo sedimentáciou a kys- lý filtrát, alebo predčistené odpadové vody sa po neutralizácii dočistia biologicky.The purpose of the invention is to eliminate the poorly stable urea-formaldehyde condensate from the effluent from the production of urea-formaldehyde adhesives, thereby eliminating the possibility of clogging of pipelines and treatment facilities. This purpose is achieved by treating the waste water from the production of urea-formaldehyde adhesives with an inorganic or organic acid to a pH of 1-5, preferably to a pH of 1.2-2. The precipitated urea-formaldehyde condensate is separated off, preferably by filtration or sedimentation, and the acidic filtrate or pre-treated wastewater is purified biologically after neutralization.

Description

1 231 3751,231,375

Vynález sa týká spósobu predčistenia odpadových vod z vý-roby močovino-formaldehydových lepidiel obsahujúcich močovino-formaldehydový kondenzát, formaldehyd a močovinu.BACKGROUND OF THE INVENTION The present invention relates to a process for the purification of waste water from the production of urea-formaldehyde adhesives comprising urea-formaldehyde condensate, formaldehyde and urea.

Močovino-formaldehydový kondenzát, ktorý sa nachádza v od-padových vodách z výroby močovino-formaldehydových lepidiel; jenestabilný, vypadává z roztoku a zalepuje dopravné tra$y. Volnýformaldehyd je toxický zvlášť pre následovně biologické čistenieodpadových vód.Urea-formaldehyde condensate found in wastewater from urea-formaldehyde adhesives; just stable, falling out of solution and sealing transport trails. Freeformaldehyde is particularly toxic for subsequent biological treatment of waste water.

Odpadové vody s vyšším obsahom formaldehydu sa v mnohýchprípadoch čistia fyzikálno-chemickými postupmi, Katalytickou oxi-daci ou peroxidom vodíka v přítomnosti kovového železa, soli že-leza, iných soli alkalických kovov, alebo kov ov alkalických ze-min, platiny /japonské přihlášky vynálezov 44 906/72, 111 085/81,24 694/82, patent ZS3R 552309, patenty NSR 2703267, 2703268/,oxidáciou chlórnanom v přítomnosti oxidu nikelnatého na PVC no-siči /japonská přihláška vynálezu 27075/80/·Wastewater with a higher formaldehyde content is in many cases purified by physico-chemical processes, by catalytic oxidation of hydrogen peroxide in the presence of iron metal, salt of iron, other alkali metal salts, or metal of alkaline minerals, platinum / Japanese patent applications 44 906/72, 111 085 / 81,24 694/82, patent ZS3R 552309, patents NSR 2703267, 2703268 /, oxidation of hypochlorite in the presence of nickel oxide on PVC carrier (Japanese Patent Application 27075/80) ·

Známe sú tiež spósoby biologického čistenia odpadových vóds vyšším obsahom volného formaldehydu aktivovaným kalom /patentZjSSR 792214/, Československé autorské osvedčenie 169 239 uvádzachemický spósob detoxikácie a predčistenia odpadových véd z vý-roby močovino-formaldehydových lepdiel aldolizáciou formaldehy-du a čiastočným vyzrážaním močovino-formaldehydového lepidla valkalickej oblasti pri ^eplote 40 - 90 °C.Also known are methods for the biological purification of waste water with higher free formaldehyde activated sludge content (U.S. Pat. No. 792214); at a temperature of 40-90 ° C.

Bolo zistené, že odpadové vody znečistěné volným formalde-hydom možno s vysokou účinnosťou čistit* adaptovaným aktivovanýmkalom pri koncentraciách 200 - 2 000 mg.1*"1. Preto jedným z hlav-ných problémov, ktoré gznikajú pri čistění odpadových vod z vý-roby močovino-formaldehydových lepidiel je zanášanie dopravnýchtrás a čistiacich zariadení vypadnutým močovino-formaldehydovýmkondenzátom. 2 231 373It has been found that waste waters contaminated with free formaldehyde can be purified with high efficiency by adapted activated alkaline at concentrations of 200-2,000 mg / m @ -1. Therefore, one of the major problems encountered in the purification of wastewater from production of urea-formaldehyde adhesives is the clogging of traffic routes and cleaning equipment with fallen urea-formaldehyde condensate.

Vyášie uvedené problémy odstraňuje použitie nového postupupredčistenia odpadových vód·The above mentioned problems eliminate the use of a new waste water purification process ·

Vynález sa týká spósobu predčistenia odpadových vód z výro-by močovino-formaldehydových lepidiel obsahujúcich močovino-£ormaldehydový kondenzát, formaldehyd a močovinu. Odpadové sodyz výroby močovino-f ormaldehydových lepidiel sa upravia anorganic-kou, alebo organickou kyselinou s výhodou kyselinou chlorovodí-kovou, sirovou, alebo mravčou na pU 1-5, s výhodu na pH 1,2-2.BACKGROUND OF THE INVENTION The present invention relates to a process for the purification of waste water from the production of urea-formaldehyde adhesives comprising urea-formaldehyde condensate, formaldehyde and urea. Waste soda ash for the production of urea-formaldehyde adhesives is treated with an inorganic or organic acid, preferably hydrochloric acid, sulfuric acid or formic acid, preferably at pH 1.2-2.

Po spparácii vypadnutého močovino-formaldehy«|ového kondenzátu,s výhodou použitia filtrácie alebo samočinnej sedimentácie, safiltrát alebo predčistené odpadové vody dočistia biologicky· Výhodné je použit predčistené kyslé vody na acidický rozkladodpadových vód obsahujúcich v kyslom prostředí nestabilně zlúče-niny formaldehydu, napr· hexametylentetramín, dinitrozopentame-tylentetramín· Z hlediska technologie výroby močovino-formaldehydových le-pidiel je hlavnou výhodou spósobu predčisťovania odpadových vódpodlá tohto vynálezu vylúčenia možnosti zanášania potrubí kana-lizácie a čistiarenských zariadení močovmo-f ormaldehydovým kon-denzátom· Spósob predčistenia je velmi jednoduchý a technologickynenáročný· Příklad 1After evaporation of the precipitated urea-formaldehyde condensate, preferably the use of filtration or automatic sedimentation, the safiltrate or pre-treated wastewater is biologically purified. Preferred is the pre-treated acidic water for acidic decomposition of waste waters containing unstable formaldehyde compounds in the acidic environment, for example hexamethylentetramine , dinitrozopentame-tylentetramine · From the point of view of the urea-formaldehyde binder production technology, the main advantage of the method of wastewater pretreatment according to the invention is the elimination of the possibility of clogging of the sewage and sewage treatment plants with urea-formaldehyde condensate. Example 1

Stav před aplikáciou vynálezu. Nepredčistené odpadové vodyz výroby močovino-formaldehydových lepidiel majú následovně zlo-ženie; CHSKCr= 15 140 mg.l”1 volný formaldehyd = 550 mg.l”1 obsah dusíka = 0,58 % odpařok = 16,2 g·!"^ pH = 6,4 Čiastočne vypadnutým močovino-formaldehydovým kondenzátombolí zanesené potrubia a preto sa na čistiareň odpadových vód 231 375 prevážajú cisternovými vezmi, čo značné ekonomicky zaíažuge čia-tenie odpadových vod z výroby močovino-formaldehydových lepidiel. Příklad 2State prior to application of the invention. Untreated waste waters from the production of urea-formaldehyde adhesives have the following composition; CODCr = 15 140 mg.l ”1 free formaldehyde = 550 mg.l” 1 nitrogen content = 0.58% evaporator = 16.2 g ·! ”^ PH = 6.4 Partially dropped urea-formaldehyde condensate chamber clogged pipes are transported to the waste water treatment plant 231 375 by tank wagons, which considerably economies in wastewater treatment from the production of urea-formaldehyde adhesives.

Do piatich kadiniek s obsahom po 600 ml odpadovej vody z vý-roby močovino-formaldehydových lepidiel /vyššie uvedeného zlože-nia/ bolo přidané také množstvo kyseliny sírovéj, aby pH v Jed-notlivých kádinkách bolo 1,2> 1,4$ 1,8 a 2,7$/4,25 ml, 2 ml, 0,86 ml, 0,40 ml a 0,17 ml koncentrovanéj kyseliny sírovéj/.Into five beakers containing 600 ml of waste water from the urea-formaldehyde adhesives (above), an amount of sulfuric acid was added to bring the pH of the individual beakers to 1.2 > 1.4 $ 1, 8 and 2.7 $ / 4.25 ml, 2 ml, 0.86 ml, 0.40 ml and 0.17 ml of concentrated sulfuric acid.

Zmes bola miešaná pri cca 50 ot. min.”1. V polhodinových inter-valoch odoberané vzorky boli filtrované fritou S-4-. Vo filtrá-te bola stanovená CHSK, celkový dusík, volný formaldehyd a odparokVýsledky sú uvedené v tabulke. čas /min/ 30 60 90 120 150 CHSK /mg.l”1/ pH=l,2 6 630 5 240 4 520 4 230 4 200 CHSK /mg.l“1/ pH=l,4 7 520 6 160 5 260 4 720 4 630 CHSK /mg.l”1/ pH=l,6 8 390 7 600 6 200 5 870 5 630 CHSK /mg.l”1/ pH=l,8 10 600 8 720 8 110 7 980 7 540 CHSK /mg.l”1/ pH»2,7 15 100 15 040 14 900 14 380 13 290 H /%/ pH-1,4 «« 0,20 - 0,15 - 0,13 odparok/g.l”1/ pH=l,4 6,7 - 4,3 - 3,6The mixture was stirred at ca. min. ”1. Samples taken at half-hour intervals were filtered with S-4- frit. COD, total nitrogen, free formaldehyde and residue were determined in the filtrate. Results are shown in the table. time / min / 30 60 90 120 150 COD /mg.l”1/ pH = 1, 2 6 630 5 240 4 520 4 230 4 200 COD /mg.l"1/ pH = 1, 4 7 520 6 160 5 260 4 720 4 630 COD /mg.l”1/ pH = 1, 6 8 390 7 600 6 200 5 870 5 630 COD /mg.l”1/ pH = 1, 8 10 600 8 720 8 110 7 980 7 540 COD /mg.l”1/ pH »2.7 15 100 15 040 14 900 14 380 13 290 H /% / pH-1.4« «0.20 - 0.15 - 0.13 evaporator / gl 1 (pH = 1.4) 6.7 - 4.3 - 3.6

Koncentrácia volného formaldehydu sa u jednotlivých vzoriekpočas experiment ov výraznéjšie neměnila. - 4 Příklad 3 231 375The free formaldehyde concentration did not change significantly over the individual samples during the experiment. Example 3 231 375

Do dvoch kadiniek s obsahom po 600 ml odpadovéj vody z vý-roby močovino-formaldehydových lepldiel bolo přidané také mno-žstvo kyseliny mravčej, aby pH v jednotlivých kádinkách bolo1,7 a 2,1 /30 ml a 3ml 80 %-nej kyseliny mravčej/. Zmes bolamiešaná pri cca 50 ot. min“'’*. V polhodinových intervalech odo-berané vzork y boli filtrované fritou S-4 a vo filtráte bola sta-novená CHSK. Výsledky sú uvedené v tabu!ke. cas /min./ CHSK /mg.l“1/CHSK /mg.l“1/ 30 60 90 120 150 pH«l,7 9 860 8 500 80 050 7 630 7 420 pH«2,l 12 540 11 060 10 200 9 850 9 300 tfTwo volumes of formic acid were also added to two beakers containing 600 ml of waste water from the urea-formaldehyde production to give 1.7 and 2.1 / 30 ml and 3 ml of 80% formic acid in each beaker. /. The mixture boiled at about 50 rpm. min “'” *. At half-hour intervals, the sampled samples were filtered with S-4 frit and COD was determined in the filtrate. The results are shown in Table. time / min / COD /mg.l"1/CHSK /mg.l"1/30 60 90 120 150 pH «l, 7 9 860 8 500 80 050 7 630 7 420 pH« 2, l 12 540 11 060 10,200 9,850 9,300 tf

Claims (1)

Predmet vynálezu 231 375Object of the invention 231 375 Sposob predčistenia odpadových vod z výroby močovino-formaldehydovýoh lepidiel obsahujúcioh močovino-formaldehydový kondenzát, formaldehyd a močovinu vyznačujúci sa tým, že odpadové vody sa upravia anorganickou, alebo organickou kyselinou s výhodou kyselinou chlorovodíkovou, kyselinou sírovou, alebo kyselinou raravčou na pH 1-5, s výhodou na pH 1,2-2, po zhomogeni zování zmesi sa vypadnutý kondenzát odseparuje, s výhodou filtráciou, alebo sedimentáciou·Waste water pretreatment process for the production of urea-formaldehyde adhesives comprising urea-formaldehyde condensate, formaldehyde and urea, characterized in that the wastewater is treated with an inorganic or organic acid, preferably hydrochloric acid, sulfuric acid, or scavenger acid, to a pH of 1-5, preferably to a pH of 1.2-2, after homogenization of the mixture, the precipitated condensate is separated, preferably by filtration or sedimentation.
CS829706A 1982-12-27 1982-12-27 The method of pre-treatment of wastewater from the production of urea-formaldehyde adhesives CS231375B1 (en)

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