HU185194B - Method for detoxication mixing tannery sewage sludges - Google Patents
Method for detoxication mixing tannery sewage sludges Download PDFInfo
- Publication number
- HU185194B HU185194B HU82100A HU10082A HU185194B HU 185194 B HU185194 B HU 185194B HU 82100 A HU82100 A HU 82100A HU 10082 A HU10082 A HU 10082A HU 185194 B HU185194 B HU 185194B
- Authority
- HU
- Hungary
- Prior art keywords
- sludge
- heavy metal
- acid
- sulfuric acid
- slurry
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 10
- 239000010865 sewage Substances 0.000 title claims 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 14
- 239000010802 sludge Substances 0.000 claims abstract description 14
- 239000002253 acid Substances 0.000 claims abstract description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 9
- 239000010801 sewage sludge Substances 0.000 claims abstract description 9
- 239000002002 slurry Substances 0.000 claims abstract description 8
- 231100000331 toxic Toxicity 0.000 claims abstract description 8
- 230000002588 toxic effect Effects 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 5
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 5
- 239000004571 lime Substances 0.000 claims abstract description 5
- 238000005406 washing Methods 0.000 claims abstract description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 3
- 229910052751 metal Inorganic materials 0.000 claims abstract description 3
- 239000002184 metal Substances 0.000 claims abstract description 3
- 239000011707 mineral Substances 0.000 claims abstract description 3
- 239000008267 milk Substances 0.000 claims description 4
- 210000004080 milk Anatomy 0.000 claims description 4
- 235000013336 milk Nutrition 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 239000011368 organic material Substances 0.000 claims description 3
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 229910021432 inorganic complex Inorganic materials 0.000 claims description 2
- 230000020477 pH reduction Effects 0.000 claims description 2
- 230000002500 effect on skin Effects 0.000 claims 1
- 229910021645 metal ion Inorganic materials 0.000 claims 1
- 239000000725 suspension Substances 0.000 abstract description 9
- 150000002500 ions Chemical class 0.000 abstract description 4
- 239000010985 leather Substances 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 239000003929 acidic solution Substances 0.000 abstract 1
- 150000007513 acids Chemical class 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000011651 chromium Substances 0.000 description 3
- 229910001430 chromium ion Inorganic materials 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical class [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- WLZRMCYVCSSEQC-UHFFFAOYSA-N cadmium(2+) Chemical compound [Cd+2] WLZRMCYVCSSEQC-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/529—Processes or devices for preparing lime water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/004—Sludge detoxification
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/303—Complexing agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/22—Nature of the water, waste water, sewage or sludge to be treated from the processing of animals, e.g. poultry, fish, or parts thereof
- C02F2103/24—Nature of the water, waste water, sewage or sludge to be treated from the processing of animals, e.g. poultry, fish, or parts thereof from tanneries
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Removal Of Specific Substances (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Die Erfindung betrifft ein Verfahren zur entgiftenden Behandlung und gegebenfalls zur Verwertung von toxische Schwermetallkomplexe und organische Stoffe enthaltendem Abwasserschlamm der Industrie, insbesondere der Lederindustrie, bei dem man den Abwasserschlamm unter Verischen mit Wasser zu einer hoechstens 100kg/m hoch 3, vorzugsweise 20 bis 40kg/m hoch 3 Feststoffe enthaltenden Abwasserschlamm-Suspension homogenisiert, die erhaltene Suspension mit Schwefelsaeure oder mit einem mindestens 30% Schwefelsaeure enthaltenden Mineralsaeure-Gemisch derart versetzt, dass die Saeurekonzentration der Schlammsuspension dabei 10Gew.-% nicht ueberschreitet und der pH-Wert der Suspension nach Beendigung der Saeurezugabe unter 1 bleibt, woraufhin man das angesaeuerte Gemisch bei 20 Grad bis 100 Grad C zur Zersetzung der Schwermetallkomplexe ruehrt, die die entstehendenen Schwermetatallsalze enthaltende saure Loesung von dem Schlamm trennt und zweckmaessig mit Kalkmilch neutralisiert. DieMetallsalze werden dann bei einem pH von 8 bis 10 ausgefaellt, und der abgetrennte Schlamm wird durch Waschen von den Schwermetallionen und Saeuren befreit.The invention relates to a method for detoxifying treatment and optionally for the recovery of toxic heavy metal complexes and organic sewage sludge containing industry, in particular the leather industry, in which the sewage sludge mixed with water to a maximum of 100kg / m high 3, preferably 20 to 40kg / homogenized, the resulting suspension with sulfuric acid or containing at least 30% sulfuric acid mineral acid mixture such that the acid concentration of the sludge suspension does not exceed 10Gew .-% and the pH of the suspension after completion the acid addition remains below 1, whereupon the acidified mixture is stirred at 20 degrees to 100 degrees C to decompose the heavy metal complexes, which separates the resulting acidic solution containing heavy metal salts from the slurry and expediently neutralized with lime. The metal salts are then precipitated at a pH of 8 to 10, and the separated sludge is freed from the heavy metal ions and acids by washing.
Description
A találmány tárgya eljárás toxikus nehézfémsó komplexeket és szervesanyagokat tartalmazó, előnyösen bőrgyári iszapok méregtelenítő kezelésére és adott esetben hasznosítására.The present invention relates to a process for the detoxification treatment and optionally utilization of toxic heavy metal salt complexes and organic materials, preferably dermatological sludges.
A nyersbőrök cserzése, kikészítése során 80-95 % víztartalmú szennyvíziszap keletkezik, amely nagy szervesanyag tartalma következtében kiváló növényi tápanyagot jelenthetne, azonban a gyártástechnológiában alkalmazott vegyszerek nehézfém-ion - gyakran jelentős króm-ion — tartalma az iszapba kerülve azt toxikus hatásúvá teszi.During tanning and dressing of hides, 80-95% water-containing sewage sludge is produced, which, due to its high organic content, can provide excellent plant nutrients, but the heavy metal ions - often significant chromium ions - used in manufacturing technology render them toxic.
Az iszap égetése a nagy víztartalom miatt gazdaságtalan. Számos eljárás ismeretes különböző flokkuláló szerek alkalmazásával a kolloidális elosztású szervesanyagok tömörítésére, szűrhetővé tételére, azonban a szennyvíziszap gazdaságos víztelenítése változatlanul megoldatlan feladat.Combustion of sludge is uneconomical due to its high water content. Many methods are known using various flocculating agents to compact and filter colloidal organic materials, but the economical dewatering of sewage sludge remains an unresolved problem.
A nagy nedvességtartalmú szennyvíziszapot általában tározó tavakban helyezik el, de a nehézfémsók toxikus hatása miatt az egyre szigorodó környezetvédelmi előírások mellett a lerakóhely kiválasztása is egyre nagyobb gondot jelent.High-moisture sewage sludge is usually deposited in reservoir ponds, but due to the toxic effects of heavy metal salts, the choice of landfill is increasingly problematic in addition to increasingly stringent environmental regulations.
Az iszap toxikus anyagainak kivonására és komponensek hasznosítására az irodalomban nem található semmilyen utalás, vagy megoldás.No references or solutions have been found in the literature for extracting toxic materials from sludge and utilizing components.
A találmány célja olyan eljárás kidolgozása, amellyel a szennyvíziszap króm- és egyéb nehézfémsó tartalma kivonható, és a szervesanyagokat tartalmazó maradék pedig az egyre növekvő környezetvédelmi követelményeknek is megfelelő, sőt mezőgazdaságilag hasznosítható formába hozható. A találmány azon a felismerésen alapul, hogy a különböző szerves és szervetlen komplex, illetve vízoldhatallan csapadék formájában levő nehézfémIt is an object of the present invention to provide a process for extracting the chromium and other heavy metal salt content of sewage sludge and converting residues containing organic matter into ever more environmentally friendly and even agriculturally useful forms. The invention is based on the discovery that heavy metals in the form of various organic and inorganic complexes and water-insoluble precipitates
- elsősorban Cr+ + + - vegyületek ásványi és legalább 30 % kénsavat tartalmazó saveleggyel végzett szabályozott hidrolízissel megbonthatok és vízoldbató formában eltávolíthatók az iszapból.- they are predominantly broken down by controlled hydrolysis of Cr + + + compounds with a mineral mixture containing at least 30% sulfuric acid and removed from the sludge in a water-soluble form.
A találmány szerinti eljárás lényege, hogy a homogenizált, maximálisan 100 kg/m3 - előnyösen 20-40 kg/ιη3 - szárazanyag tartalmú iszapot kénsavval, illetve legalább 30 % arányban kénsavat tartalmazó sósav, salétromsav, vagy foszforsav Heggyel érintkeztetjük 20- 100 °C közötti hőmérsékleten intenzív keverés közben oly módon, hogy a savkoncentráció a szuszpenzióban az adagolás közben ne haladja meg a 10 s% értéket és a kémiai reakciók lejátszódása után az oldat pH-ja I érték alá csökkenjenThe process according to the invention comprises contacting the homogenized sludge with a maximum solids content of 100 kg / m 3 , preferably 20-40 kg / ιη 3 , with sulfuric acid, hydrochloric acid, nitric acid or phosphoric acid containing at least 30% sulfuric acid at 20-100 ° C. C, with vigorous stirring, so that the acid concentration in the suspension does not exceed 10% by weight during the addition and the pH of the solution drops below I after chemical reactions have occurred.
Amennyiben a szuszpenzió koncentrációja meghaladja a jelzett értéket, a savazáskor stabil hab képződhet, amely a kémiai reakció sebességét lényegesen lelassítja.If the concentration of the suspension exceeds the indicated value, a stable foam may be formed upon acidification, which will significantly slow down the rate of the chemical reaction.
Ha a komplexek bontásához alkalmazott sav vagy sav-elegy nem tartalmaz kénsavat, a szuszpenzió későbbi elválasztása, ülepítése, szűrése lényegesen nehezebb művelet, mint kénsav jelenlétében.If the acid or acid mixture used for the decomposition of the complexes does not contain sulfuric acid, the subsequent separation, sedimentation and filtration of the suspension is much more difficult than in the presence of sulfuric acid.
A komplexek bomlási sebessége már szobahőmérsékleten is kielégítő, ezért a reakció a szuszpenzió adott hőmérsékletén is végbemegy, a műveletnek külön hőigénye nincs, de természetesen a hőmérséklet emelése a reakció sebességet növeli. A hőmérséklettől függő reakcióidő után a szusz2 penzió szilárdanyag tartalmát koncentráljuk, pl. telepítéssel vagy arparátorban vízzel vagy híg kénsavval nehézfém-ion mentesre mossuk, mésztejjel semlegesítjük és elválasztjuk az oldattól. Az iszaptól elválasztott oldat nehézfém-só tartalmát csapadékképzéssel koncentráljuk és méregtemetőbe, vagy esetleges tisztítás és szétválasztás után újbóli hasznosításra visszük. Az eljárás elvi vázlatát az 1. ábra szemlélteti.The decomposition rate of the complexes is already satisfactory at room temperature, so that the reaction proceeds at a given temperature of the suspension, the operation does not require any heat, but of course increasing the temperature increases the reaction rate. After a temperature-dependent reaction time, the suspension content of the suspension is concentrated, e.g. The product is washed with water or dilute sulfuric acid in a planter or arparator, free of heavy metal ions, neutralized with lime milk and separated from the solution. The heavy metal salt content of the solution separated from the sludge is concentrated by precipitation and recycled to a poison cemetery or after purification and separation. A schematic diagram of the process is illustrated in Figure 1.
PéldaExample
Fermentált bőrgyári szennyvíziszapot krómmentesítünk, amelynek jellemzői:Fermented leather factory sewage sludge is de-chromed with the following characteristics:
Szárazanyag tartalom: 200 kg/m3 Dry matter content: 200 kg / m 3
Szervesanyagtartalom: 100 kg/m3 Organic matter content: 100 kg / m 3
Króm-ion tartalom: 12 kg/m3 Chromium ion content: 12 kg / m 3
Az iszap nyomokban cink és kadmium ionok; valamint jelentős mennyiségben vas- és kalciumionokat is tartalmaz.The sludge contains traces of zinc and cadmium ions; as well as significant amounts of iron and calcium ions.
A feldolgozandó iszapot az 1 homogenizátorban 1 : 6 lérfogatarányban vízzel keverjük, illetve a mosó-szeparáló rendszerből származó króm-ion tartalmú savas vízzel keverjük. A kvázi homogén szuszpenziót a 2 reaktorban vezetjük, ahol 1 m3 feldolgozandó iszaphoz 150 kg 96 %-os kénsavat adagolunk és a zagy aktuális hőmérsékletén 60 perc tartózkodási időt biztosítunk intenzív keverés mellett.The slurry to be processed is mixed with water in a 1: 6 volume ratio in the homogenizer 1 or with acidic water containing chromium ion from the washer separation system. The quasi-homogeneous slurry is fed into reactor 2 where 150 kg of 96% sulfuric acid is added to 1 m 3 of sludge to be processed and a residence time of 60 minutes at the actual temperature of the slurry is maintained with vigorous stirring.
A szuszpenzió szilárdanyag tartalmát a 3 szeparátorban koncentráljuk, ahonnan a sűrített iszap a 4 mosó-elválasztó rendszerbe, majd az 5 semlegesítő-szeparáló rendszerbe kerül, amelynek kimenetén már a nehézfém-ion mentes iszap áll rendelkezésre mésztejjel semlegesítve. A 4 mosórendszerből a mosóvizet visszavezetjük az 1 homogenizátorba. A 3 szeparátorból a krómtartalmú oldatot a 6 leválasztóba vezetjük, ahol mésztej adagolással a fémsókat lecsapjuk 8—10 pH közötti érték mellett. A nehézfém-ionokat tartalmazó csapadékot a 7 szeparátorban elválasztjuk a meszes víztől.The solids content of the slurry is concentrated in the separator 3, from where the condensed sludge enters the washer separation system 4 and then into the neutralization-separator system 5, at the outlet of which the heavy metal-free sludge is neutralized with lime milk. From the washing system 4, the washing water is returned to the homogenizer 1. From the separator 3, the chromium-containing solution is introduced into the separator 6, where metal salts are precipitated by the addition of lime milk at a pH of 8 to 10. The heavy metal ions precipitate in the separator 7 is separated from the lime water.
A találmány szerinti eljárás előnyei:Advantages of the process according to the invention:
- az eljárás megoldja a bőrgyári szennyvíziszappal kapcsolatos környezetvédelmi problémákat, feleslegessé teszi a tározó tavak létesítését és mentesít a toxikus iszap szállításától;- the solution solves the environmental problems associated with the sewage sludge from the tannery, eliminates the need to build reservoirs and eliminates the need to transport toxic sludge;
- lehetővé teszi a nagy szervesanyag tartalmú iszap mezőgazdasági hasznosítását talajjavítási célokra;- enables the agricultural use of high organic sludge for soil improvement;
- lehetővé teszi a visszanyert nehézfémsó tartalmi csapadék további feldolgozásával az abban lévő értékes anyagok újbóli hasznosítását.- allows the further recovery of the valuable materials contained therein by further processing the recovered heavy metal salt precipitate.
Claims (2)
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HU82100A HU185194B (en) | 1982-01-14 | 1982-01-14 | Method for detoxication mixing tannery sewage sludges |
RO109659A RO86780B (en) | 1982-01-14 | 1983-01-10 | Process for removing heavy metal compounds from muds resulting from tanneries |
ES518907A ES518907A0 (en) | 1982-01-14 | 1983-01-11 | PROCEDURE TO DETOXICATE RESIDUAL SUSPENSIONS OF THE LEATHER INDUSTRY AND THE LIKE. |
CS83182A CS246057B2 (en) | 1982-01-14 | 1983-01-11 | Method of industrial waste detoxication with heavy metals' toxic salt complexes content |
DD83247194A DD209430A5 (en) | 1982-01-14 | 1983-01-12 | METHOD FOR THE DETOXIFIC TREATMENT OF LEATHER INDUSTRY WASTE SLUDGE |
YU00063/83A YU6383A (en) | 1982-01-14 | 1983-01-12 | Process for the detoxication of industrial wastes, containing toxic heavy metal salts |
PL1983240123A PL139584B1 (en) | 1982-01-14 | 1983-01-12 | Method of treating industrial waste waters containing complex salts of heavy metals |
IT19091/83A IT1160174B (en) | 1982-01-14 | 1983-01-13 | PROCEDURE FOR DETOXIFYING INDUSTRIAL WASTE MATERIALS CONTAINING TOXIC HEAVY METAL SALT COMPLEXES |
GB08300987A GB2113199B (en) | 1982-01-14 | 1983-01-14 | Detoxication of industrial waste |
DE19833301120 DE3301120A1 (en) | 1982-01-14 | 1983-01-14 | METHOD FOR DETOXIFYING WASTE WATER SLUDGE OF THE LEATHER INDUSTRY |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HU82100A HU185194B (en) | 1982-01-14 | 1982-01-14 | Method for detoxication mixing tannery sewage sludges |
Publications (1)
Publication Number | Publication Date |
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HU185194B true HU185194B (en) | 1984-12-28 |
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ID=10947909
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HU82100A HU185194B (en) | 1982-01-14 | 1982-01-14 | Method for detoxication mixing tannery sewage sludges |
Country Status (10)
Country | Link |
---|---|
CS (1) | CS246057B2 (en) |
DD (1) | DD209430A5 (en) |
DE (1) | DE3301120A1 (en) |
ES (1) | ES518907A0 (en) |
GB (1) | GB2113199B (en) |
HU (1) | HU185194B (en) |
IT (1) | IT1160174B (en) |
PL (1) | PL139584B1 (en) |
RO (1) | RO86780B (en) |
YU (1) | YU6383A (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3428535A1 (en) * | 1984-08-02 | 1986-02-13 | Siekmann, Helmut E., Prof.Dr.-Ing., 1000 Berlin | METHOD AND DEVICE, IN PARTICULAR FOR THE CONDITIONING OF SEWAGE SLUDGE |
DE3503199C2 (en) * | 1985-01-31 | 1987-03-19 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Process for producing a soil improver or a fertilizer from sewage sludge |
DE3627253C2 (en) * | 1986-08-12 | 1995-06-22 | Linde Ag | Process for the biological treatment of substrates containing organic substances |
DE3919788C1 (en) * | 1989-06-16 | 1990-07-05 | Siebtechnik Gmbh, 4330 Muelheim, De | |
FI97288C (en) * | 1993-08-26 | 1996-11-25 | Kemira Oy | Procedure for treatment of wastewater sludge |
ITRM20010671A1 (en) * | 2001-11-12 | 2003-05-12 | Sicit Chemitech S P A | CHROME-BASED PRODUCT IN COMPOSITION WITH HYDROLYZED PROTEINS AND PROCESS FOR ITS OBTAINING. |
AU2003900241A0 (en) * | 2003-01-21 | 2003-02-06 | Australian Organic Resources Pty Ltd | The extraction and treatment of heavy metals in sewage sludge |
ITRM20050425A1 (en) * | 2005-08-05 | 2007-02-06 | Sicit Chemitech S P A | PROCESS FOR THE PRODUCTION OF PRODUCTS BASED ON HYDRAULIC PROTEINS IN COMPOSITION WITH MANGANESE. |
JP5985925B2 (en) * | 2012-08-20 | 2016-09-06 | 水ing株式会社 | Method and apparatus for treating waste liquid containing heavy metal |
-
1982
- 1982-01-14 HU HU82100A patent/HU185194B/en not_active IP Right Cessation
-
1983
- 1983-01-10 RO RO109659A patent/RO86780B/en unknown
- 1983-01-11 ES ES518907A patent/ES518907A0/en active Granted
- 1983-01-11 CS CS83182A patent/CS246057B2/en unknown
- 1983-01-12 PL PL1983240123A patent/PL139584B1/en unknown
- 1983-01-12 DD DD83247194A patent/DD209430A5/en unknown
- 1983-01-12 YU YU00063/83A patent/YU6383A/en unknown
- 1983-01-13 IT IT19091/83A patent/IT1160174B/en active
- 1983-01-14 GB GB08300987A patent/GB2113199B/en not_active Expired
- 1983-01-14 DE DE19833301120 patent/DE3301120A1/en not_active Withdrawn
Also Published As
Publication number | Publication date |
---|---|
GB2113199A (en) | 1983-08-03 |
RO86780B (en) | 1985-05-31 |
RO86780A (en) | 1985-05-20 |
CS246057B2 (en) | 1986-10-16 |
ES8402549A1 (en) | 1984-03-01 |
PL139584B1 (en) | 1987-02-28 |
ES518907A0 (en) | 1984-03-01 |
IT8319091A0 (en) | 1983-01-13 |
DE3301120A1 (en) | 1983-07-28 |
GB8300987D0 (en) | 1983-02-16 |
YU6383A (en) | 1985-10-31 |
GB2113199B (en) | 1985-07-10 |
DD209430A5 (en) | 1984-05-09 |
PL240123A1 (en) | 1984-06-18 |
IT1160174B (en) | 1987-03-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
HU90 | Patent valid on 900628 | ||
HMM4 | Cancellation of final prot. due to non-payment of fee |