CS274068B1 - Method of waste waters final treatment from technological processes of leather tanning - Google Patents

Method of waste waters final treatment from technological processes of leather tanning Download PDF

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Publication number
CS274068B1
CS274068B1 CS260489A CS260489A CS274068B1 CS 274068 B1 CS274068 B1 CS 274068B1 CS 260489 A CS260489 A CS 260489A CS 260489 A CS260489 A CS 260489A CS 274068 B1 CS274068 B1 CS 274068B1
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Czechoslovakia
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chromium
tanning
ammonia
residual
ammoniac
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CS260489A
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Czech (cs)
Slovak (sk)
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CS260489A1 (en
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Eva Ing Csc Horvathova
Josef Ing Konecny
Jan Ing Svancer
Zdenek Ing Bosan
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Eva Ing Csc Horvathova
Josef Ing Konecny
Jan Ing Svancer
Zdenek Ing Bosan
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Priority to CS260489A priority Critical patent/CS274068B1/en
Publication of CS260489A1 publication Critical patent/CS260489A1/en
Publication of CS274068B1 publication Critical patent/CS274068B1/en

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  • Treatment Of Water By Ion Exchange (AREA)

Abstract

After mechanical-biological purification of waste water from technological processes of tanning leather, waste water containing ammoniac and increased chromium is cleaned by sorption on granular clinoptilolite. After saturation, washing with a solution of sodium chloride alkalizated by sodium hydroxide, ammoniac is eluated, stripped by air and caught on a foam absorber, which is recycled into the technology of tanning leather. Residual colmation of natural clinoptilolite by chromium is liquidated by final washing of the bed by 0.02 hydrochloric acid. Ammoniac water and the eluate with residual chromium is recycled into the technological process of tanning leather. Ammoniac and residual chromium are removed from waste water with high effectiveness.

Description

(54)(54)

274 274 06: 06: (11) (11) (13) (13) B 1 B 1 (51) (51) lni. CČ LNI. CČ c C 02 F 1/28 02 F 1/28

Spůsob dočisťovania odpadových vůd z technologických procesov vyčiňovania koží ‘ ' Po mechanicko-biologickom čistění odpadových vůd z technologických procesov vyčiňovania koží^sa odpadové vody obsahujúce amoniak a zvyškový chróm dočisťujú sorpciou na zrnitom klinoptilolite. Z prírodného klinoptilolitu sa následné, po nasýtení, premytím roztokom chloridu sodného alkalizovaným hydroxidom sodným eluuje, vzduchom vystripuje a na penovom absorbéri zachytí amoniak, ktorý do technologie vyčiňovania koží recykluje. Zvyšková kolnatácia prírodného klinoptilolitu chrómom sa likviduje finálnym premytím lůžka 0,02 kyselinou solnou. Amoniakálna voda a eluát so zvyškovým chrómom recyklujú do technologického procesu vyčiňovania koží.After mechanical-biological purification of the waste leads from the skin tanning process, the waste water containing ammonia and residual chromium is purified by sorption on granular clinoptilolite. Subsequent to saturation, it is eluted from the natural clinoptilolite by washing with a sodium chloride alkaline sodium hydroxide solution, stripped with air and trapped with ammonia on the foam absorber, which is recycled to the skin tanning technology. The residual collagation of natural clinoptilolite with chromium is eliminated by a final wash of the bed with 0.02 hydrochloric acid. Ammonia water and the residual chromium eluate are recycled to the technological process of tanning leather.

Amoniak a zvyškový chróm sa z odpadových vůd odstraňujú s vysokou účinnosťou.Ammonia and residual chromium are removed from the waste lines with high efficiency.

CS 274068 BlCS 274068 Bl

Vynález sa týká spůsobu dočisťovania odpadových vůd z technologických procesov vyčiňovania koži v koželuzníctve od amoniaku a zvyškového chrómu, s kontinuálnou recykláciou odstraňovaných látok.The invention relates to a method for purifying waste leads from technological processes of tanning leather in tanneries from ammonia and residual chromium, with the continuous recycling of the removed substances.

Amoniak sa v technologickom procese vyčiňovania koži v koželužníctve používá na koaguláciu a chemická zrážanie Cr(OH), - ČSSR patent 124 395 ako vhodné činidlo, ktoré dokᣠ* že udržiavať požadované pH = 8 prostredia regeneračných brečiek.Ammonia is used for the coagulation and chemical precipitation of Cr (OH) in the tanning process of the tanning industry, as a suitable agent which can maintain the desired pH = 8 of the regenerative sludge environment.

Oůsledkom používania amoniaku je však na druhej straně skutočnosť, že v odpadových vodách z technologických procesov vyčiňovania koži je i po ich mechanicko-biologickom čistění z hladiska priameho vypúsťania do recipientu, často nepřípustné vysoký obsah amoniaku. Mechanicko-biologické čistenie týchto odpadových vůd tiež nepostačuje na odstraňovanie zvyškového chrómu, ktorý je inhibítorom biologického čistenia.On the other hand, the consequence of the use of ammonia is that in the waste water from the technological processes of skin tanning, even after their mechanical-biological purification from the point of direct discharge into the recipient, often high ammonia content is inadmissible. The mechanical-biological purification of these waste leaders is also not sufficient to remove residual chromium, which is an inhibitor of biological purification.

Teraz sa zistilo, že amoniak a zvyškový chróm je možné z odpadových vůd z technologických procesov vyčiňovania koží v koželužníctve výhodné odstraňovat spůsobom ich dočisťovania s recykláciou odstraňovaných látok podía vynálezu.It has now been found that ammonia and residual chromium can be advantageously removed from the waste leaders of the tanning process of the tanning industry by purifying them with the recycling of the substances removed according to the invention.

Podstata vynálezu spočívá v tom, že odpadové vody sa po ich mechanicko-biologickom čistění podrobia dočisteniu sorpciou na zrnitom prirodnom klinoptilolite so zrnitosťou 0,3 až 1 mm, při špecifickom objemovom zatažení do 15 h'1. Z prirodného klinoptilolitu sa následné,, po nasýtení, premytím roztokom chloridu sodného, alkalizovaným hydroxidom sodným, eluuje a vzduchom vystripuje a absorpciou do vody zachytí odvětraný amoniak. Zvyšková kolmatácia prirodného klinoptilolitu chrómom sa likviduje finálnym premytím lůžka 0,02 N kyselinou solnou. Získaná amoniakálna voda a duát so zvyškovým chrómom recyklujú do technologického procesu vyčiňovania koží.The principle of the invention is that after their mechanical-biological treatment, the waste water is subjected to a sorption treatment on a granular natural clinoptilolite with a grain size of 0.3 to 1 mm, with a specific volume load up to 15 h -1 . Following saturation, washing, washing with sodium chloride solution, alkalized sodium hydroxide, elution is carried out from the natural clinoptilolite and stripped with air and absorbed into the water to absorb vented ammonia. The residual colmatation of natural clinoptilolite with chromium is eliminated by a final wash of the bed with 0.02 N hydrochloric acid. The obtained ammonia water and duct with residual chromium are recycled to the technological process of tanning leather.

Postupom podía vynálezu odstraňuje sa z odpadových vůd s vysokou účinnosťou amoniak i zvyškový chróm.The process according to the invention removes both ammonia and residual chromium from the high-efficiency waste lines.

Jeho využitie představuje materelovo uzavretý systém prevádzky, pričom zachytený amoniak je možné okrem priameho využitia v technologickom procese vyčiňovania koží využit napr. pri výrobě umělého hnojivá.Its use is a material-closed system of operation, while the trapped ammonia can be used in addition to direct use in the technological process of tanning leather, for example. in the production of fertilizer.

Prírodný klinoptilolit je z domácích zdrojov. Dočisťovanie odpadových vůd sorpciou na prirodnom klinoptilolite spůsobom podía vynálezu je investičně i prevádzkovo výhodné.Natural clinoptilolite is indigenous. Purification of the waste leaders by sorption on the natural clinoptilolite in accordance with the invention is investment and operationally advantageous.

Predmet vynálezu ilustruje ale neobmedzuje nasledujuci příklad.The present invention is illustrated but not limited by the following example.

Oočisťovala sa koželužská odpadová voda, ktorej priemerné hodnoty ukazovatelov zne-Tannery waste water was treated, the average values of indicators

čistenia boli následovně: the cleanings were as follows: PH PH 7,4 7.4 nerozpustné látky insoluble matter 33 mg.l'1 33 mg.l -1 rozpustné látky (cel) soluble substances (cel) 1200 mg.l'1 1200 mg.l -1 bsk5 bsk 5 17 mg 02.l17 mg 0 2 .l ChSKCr COD Cr 108 mg 02.1 108 mg 02.1 40-60 mg.l 40-60 mg.l Cl Cl 301 mg.l'1 301 mg.l -1 so2'Sat 2 ' 156 mg.l'1 156 mg.l -1 Cr3+ Cr 3+ 2,4 mg.l'1 2.4 mg.l -1

CS 274068 Bl *CS 274068 Bl *

Dočišťovanie sa uskutečnilo v poloprevádzkovom rozsahu v Pokusnej jednotke ČOV.Purification was carried out in the pilot plant range in the WWTP Experimental Unit.

Sorpcia prebiehala na zrnítom príródnom klinoptilolite s velkosťou zrnenia 0,3 až 1 mm umiestnenom v dvoch tlakových filtroch s prietokom do 1 m5 h\ Na desorpciu sa použil 2% chlorid sodný alkalizovaný a hydroxidom sodným. Eluáty sa zachytávali v akumulačných nádržiach, následné sa podrobili stripovaniu vzduchom a odvětraný amoniak sa zachytával do vody na penovom absorbéri. Získaná amoniakálně voda recyklovala do technologie vyčiňovania. Kolmatácia klinoptilolitu chrómom sa likvidovala premytím lůžka v oboch filtroch 0,02 N kyselinou solnou. ZvySkový chróm sa číastočne tiež zachytával v eluáte, ktorý recykloval do technologického procesu vyčiňovania koži.The sorption was carried out on granular natural clinoptilolite with a particle size of 0.3 to 1 mm placed in two pressure filters with a flow rate of up to 1 m 5 h. The eluates were collected in accumulation tanks, subsequently subjected to air stripping and the vented ammonia was collected in water on a foam absorber. The ammonia water obtained was recycled to the tanning technology. Chromium clinoptilolite collation was eliminated by washing the bed in both filters with 0.02 N hydrochloric acid. Residual chromium was also often trapped in the eluate, which was recycled to the technological process of tanning the skin.

Technologické charakteristiky poloprevádzkovóho dočiaťovania odpadovej vody zeolitom v PO ČOV Otrokovice:Technological characteristics of semi-operational waste water treatment with zeolite in WWTP Otrokovice:

Specifické objemové zaťaženie filtrov objem zeolitu vo filtri (VQ) zrnitost’ použitého zeolitu iónovýmenná kapacita k NHÍSpecific volumetric load of filters zeolite volume in filter (V Q ) grain size of zeolite used ion exchange capacity to NH1

12,B V/VQ . h'1 70 112, BV / V Q. h ' 1 70 1

0,3 - 1,0 mm ca. 10 rng.g!0.3 - 1.0 mm ca. 10 rng.g!

dl’žka pracovného cyklu v hod. 20 vo V/VQ 260 regenerácia frakčná v hod. 2,5 objem prečistenej vody v 1 cykle 18 m5 frakčný podiel regenerantu pre air-stripping 0,75 m5 spotřeba vzduchu na vystripovanie NHj (T=20 °C) ca. 20 m\lworking cycle length in hours 20 in I / O Q 260 regeneration fractional in hr. 2.5 volume of purified water per cycle 18 m 5 fraction of regenerant for air-stripping 0.75 m 5 air consumption for NH3 stripping (T = 20 ° C) ca. 20 m \ l

Využitie spůsobu dočisťovania odpadových vůd z vyčiňovania koži umožňuje materiálovo uzavretý, investičně výhodný systém prevádzky.The utilization of the method of purifying the waste lines from the tanning of the skin enables a material-closed, investment-friendly operation system.

Claims (2)

PREDMET VYNÁLEZUOBJECT OF THE INVENTION Spůsob dočisťovania odpadových vůd z technologických prccesov vyčiňovania koži v koželužníctve od amoniaku a zvyškového chrómu, s kontinuálnou recykláciou odstraňovaných látok, vyznačený tým, že sa tieto odpadové vody po mechanicko-biologickom čistění dočisťujú sorpciou na zrnitom prírodnom klinoptilolite so zrnitosťou 0,3 - 1 mm pri špecifickom objemovom zatažení 15 h^, z ktorého sa následné, po nasýtení, premytím roztokom chloridu sodného alkalizovaným hydroxidom sodným, eluuje, vzduchom vystrlpuje a absorpciou do vody zachytí odvětraný amoniak, zvySková kolmatácia prírodne'ho klinoptilolitu chrómom sa likviduje finálnym premytím lůžka 0,02 N kyselinou solnou, pričom získaná amoniakálna voda a eluát so zvyškovým chrómom recyklujú do technologického procesu vyčiňovania koži.The method of purification of waste leaders from technological processes of tanning of leather in tanneries from ammonia and residual chromium, with continuous recycling of removed substances, characterized in that these waste waters after mechanical-biological treatment are purified by sorption on granular natural clinoptilolite with a grain size of 1 mm at a specific volumetric load of 15 h ^, from which, after saturation, washing with sodium chloride solution, alkalized with sodium hydroxide, elutes, expelled by air and entrained by absorption into the water vented ammonia; 02 N hydrochloric acid, whereby the obtained ammonia water and the eluate with residual chromium are recycled into the technological process of skin tanning.
CS260489A 1989-04-27 1989-04-27 Method of waste waters final treatment from technological processes of leather tanning CS274068B1 (en)

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