SK283567B6 - Waste water treatment plant - Google Patents
Waste water treatment plant Download PDFInfo
- Publication number
- SK283567B6 SK283567B6 SK1411-97A SK141197A SK283567B6 SK 283567 B6 SK283567 B6 SK 283567B6 SK 141197 A SK141197 A SK 141197A SK 283567 B6 SK283567 B6 SK 283567B6
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- Slovakia
- Prior art keywords
- filters
- filter
- shaft
- cleaning device
- sand bed
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/04—Aerobic processes using trickle filters
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1242—Small compact installations for use in homes, apartment blocks, hotels or the like
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
Vynález sa týka čistiaceho zariadenia podľa úvodnej časti prvého nároku.The invention relates to a cleaning device according to the preamble of the first claim.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Pri odstraňovaní odpadových vôd, hlavne z decentralizovane umiestnených rodinných domov alebo dvojdomov alebo najmenších sídlisk s väčšinou menej ako desiatimi rodinnými domami, väčšinou vyvstáva problém, že pripojenie na centrálne čistiace zariadenie odpadových vôd je možné len pomocou veľmi dlhého kanalizačného potrubia za tomu zodpovedajúcich vysokých nákladov. Často používané vsakovacie jamy, v ktorých sa môže nespracovaná odpadová voda vsakovať, na druhej strane predstavujú značné zaťaženie prostredia a už sa nepovoľujú.When disposing of wastewater, especially from decentralized detached houses or semi-detached houses or smallest housing estates with mostly less than ten single-family houses, the problem usually arises that connection to a central sewage treatment plant is possible only with very long sewage pipes with corresponding high costs. Frequently used infiltration pits, in which the untreated waste water can be infiltrated, on the other hand, represent a significant environmental burden and are no longer permitted.
Pri izolovaných kalových zberných nádržkách, ktoré sa často budujú pre takéto najmenšie sídliská alebo rodinné domy, vyvstáva často problém, že sa musia v zodpovedajúcich intervaloch vyprázdňovať a obsah sa musí prepravovať a spracovávať, čo je spojené so značnými nákladmi. Okrem toho existuje nebezpečenstvo, že sa kalová zberná nádržka stane netesnou.Insulated sludge collecting tanks, which are often built for such smallest housing estates or family houses, often have the problem that they must be emptied at appropriate intervals and the contents must be transported and processed, which entails considerable costs. In addition, there is a risk that the sludge collector tank will leak.
Z FR-A-2 518 523 je známe čistiace zariadenie uvedeného druhu, pri ktorom sú na oporách prepúšťajúcich vodu nad sebou usporiadané filtre z penového plastu. Pritom sú opory filtrov stohované nad sebou pri nechaní vetraného medzipriestoru.FR-A-2 518 523 discloses a cleaning device of the type described in which foam plastic filters are arranged one above the other on the water-permeable supports. The filter supports are stacked one above the other while leaving the ventilated intermediate space.
Pri tomto známom riešení však vyvstáva problém, že na výmenu filtrov, ktoré opory držia navzájom oddialené, sa musia filtre vymeniť a opäť postaviť na seba. Prakticky je možná len výmena všetkých filtrov zároveň.In this known solution, however, the problem arises that, in order to replace the filters which hold the supports apart, the filters must be replaced and placed on top of each other. In practice, it is only possible to replace all filters at the same time.
Ďalej je známe z AT-B-391 125 čistiace zariadenie, pri ktorom sa stohujú na seba nosné sekcie s dnom prepúšťajúcim vodu a aspoň čiastočne zvýšeným okrajom. Tieto nosné sekcie sú potiahnuté prírezom z plastu a na ňom uloženou vrstvou štrku alebo piesku, ktoré spolu tvoria filter.Furthermore, a cleaning device is known from AT-B-391 125, in which the supporting sections are stacked with a water-permeable bottom and at least a partially raised edge. These support sections are coated with a plastic blank and a layer of gravel or sand deposited thereon, which together form a filter.
Pritom rovnako vyvstáva problém, že pri výmene filtra sa rovnako musia nosné sekcie oddeliť od seba a vrstvy, tvoriace vždy jeden filter, sa musia odstrániť a obnoviť, načo sa musí na každú nosnú sekciu usporiadať nový filter.There is also the problem that, when replacing the filter, the support sections must also be separated from each other, and the layers constituting each filter must be removed and renewed, and a new filter must be arranged on each support section.
V obidvoch prípadoch jc takáto výmena filtra spojená so značnými nákladmi.In both cases, such a filter change entails considerable costs.
Podstata vynálezuSUMMARY OF THE INVENTION
Cieľom vynálezu je odstrániť tieto nevýhody a navrhnúť čistiace zariadenie úvodom uvedeného druhu, ktoré sa vyznačuje jednoduchou konštrukciou a prevádzkou.It is an object of the invention to overcome these disadvantages and to propose a cleaning device of the kind mentioned at the outset, which is characterized by simple construction and operation.
Toto sa podľa vynálezu dosiahne pri zariadení úvodom uvedeného druhu znakmi význakovej časti prvého nároku.According to the invention, this is achieved in an apparatus of the foregoing kind by the features of the characterizing part of the first claim.
Pomocou navrhnutých opatrení je možné filter jednoduchým spôsobom vymeniť. Pritom stačí filter navinúť a vybrať. Tým sa získa tiež tá výhoda, že pri navíjaní filtra sa z neho vytlačí voda. Pretože filtre sú zo sklenenej alebo minerálnej vlny, je možné s nimi jednoducho manipulovať. Pri zakladaní nových filtrov, ktoré sú výhodne vytvorené ako pravouholníky, je možné ich jednoducho rozprestrieť na nosnú sekciu. Okrem toho poskytujú navrhnuté filtračné materiály veľmi dobré životné podmienky mikroorganizmom, potrebným na odbúravanie škodlivých látok v odpadovej vode.The proposed measures make it easy to replace the filter. Just wind up and remove the filter. This also gives the advantage that water is forced out of the filter during winding. Because the filters are made of glass or mineral wool, they are easy to handle. When inserting new filters, which are preferably formed as rectangles, they can be simply spread on the support section. In addition, the proposed filter materials provide very good living conditions for the microorganisms necessary for the degradation of harmful substances in waste water.
Pomocou znakov nároku 2 sa získa veľmi jednoduchá konštrukcia. Pritom je tiež možné vymieňať len jednotlivé filtre. Okrem toho sa ušetrí tiež konštrukcia nosných sekcií na filtre, ktoré sú potrebné pri známych riešeniach.By means of the features of claim 2 a very simple construction is obtained. It is also possible to replace only individual filters. In addition, the design of the filter support sections required for the known solutions is also saved.
Pomocou znakov nároku 3 sa získa veľmi kompaktná konštrukcia čistiaceho zariadenia.By means of the features of claim 3, a very compact construction of the cleaning device is obtained.
Pomocou znakov navrhnutých v nároku 4 získajú filtre vysokú mechanickú pevnosť a môžu prijať pomerne veľký objem vzduchu.By means of the features proposed in claim 4, the filters obtain high mechanical strength and can receive a relatively large volume of air.
Pomocou znakov nároku 5 je zaistená veľká miera čistoty vody, ktorá sa dostane do vsakovacej šachty.By means of the features of claim 5, a high degree of water purity is ensured which enters the infiltration shaft.
Pomocou znakov nároku 6 možno dosiahnuť obzvlášť vysoký stupeň vyčistenia spracovávaných odpadových vôd.By means of the features of claim 6, a particularly high degree of purification of the treated waste water can be achieved.
Prehľad obrázkov na výkresochBRIEF DESCRIPTION OF THE DRAWINGS
Vynález bude bližšie vysvetlený pomocou výkresov, na ktorých predstavuje obr. 1 schematicky čistiace zariadenie, obr. 2 schematicky rez predčisťovacím a usadzovacím zariadením pozdĺž čiary II - II na obr. 1, obr. 3 schematicky pozdĺžny rez stupňom biologického čistenia a obr. 4 priečny rez stupňom biologického čistenia.BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows schematically a cleaning device, FIG. 2 schematically shows a section through the pretreatment and settling device along line II-II in FIG. 1, FIG. 3 schematically a longitudinal section through the biological purification stage; and FIG. 4 is a cross-sectional view of the biological purification step.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Čistiace zariadenie podľa obr. 1 má predčisťovacie a usadzovacie zariadenie 1, zapustené do zeme, do ktorého ústi prítok 2. Predčisťovacie a usadzovacie zariadenie 1 má v podstate tri komory 3, 4 a 5, pričom z poslednej vedie odtoková rúrka 6, opatrená vetracím nátrubkom 7.The cleaning apparatus of FIG. 1 has a pre-cleaning and settling device 1 embedded in the ground into which the inlet 2 flows. The pre-cleaning and settling device 1 has basically three chambers 3, 4 and 5, the last of which is a drain pipe 6 provided with a ventilation sleeve 7.
Jednotlivé komory 3, 4 a 5 sú rozdelené pomocou steny 8, ktorá sa rozprestiera v podstate pozdĺž tetivy v podstate valcového predčisťovacieho a usadzovacieho zariadenia 1 a steny 9, ktorá prebieha v podstate kolmo na stenu 8. V oblasti komory 4 má stena 8 vo svojej najvyššej oblasti otvory 10, cez ktoré môže prúdiť odpadová voda 9, zbavená hrubších pevných látok, do komory 4. Hrubšie pevné látky sú zadržiavané v komore 3, kde môžu vypadávať a usadzovať sa ako kal.The individual chambers 3, 4 and 5 are divided by a wall 8 which extends substantially along the web of the substantially cylindrical pretreatment and settling device 1 and a wall 9 which extends substantially perpendicular to the wall 8. In the region of the chamber 4, the wall 8 has apertures 10 through which waste water 9, free of coarser solids, can flow into chamber 4. Coarser solids are retained in chamber 3 where they can fall out and settle as sludge.
V komore 4 sa môžu usadzovať jemnejšie pevné látky, takže odpadová voda, v podstate zbavená pevných látok, môže pretekať otvormi 11, usporiadanými v najvyššej oblasti steny 9, do komory 5.In the chamber 4 finer solids can settle so that the waste water, substantially free of solids, can flow through the openings 11 arranged in the highest region of the wall 9 into the chamber 5.
Pretože predčisťovacie a usadzovacie zariadenie 1 má odvetranie 12, je k dispozícii dosť vzduchu, a tým i kyslíka na hnilobné procesy. Pritom je prostredníctvom výšky pádu medzi ústím prítoku 2 a vodnou hladinou v komore, ktorá je určená umiestnením nasávacieho otvoru odtokovej rúrky 6, zaistený zodpovedajúci pohyb vodnej hladiny pri každom prítoku odpadovej vody, čím je zlepšené prevzdušnenie odpadovej vody.Since the pre-cleaning and settling device 1 has a vent 12, enough air and hence oxygen is available for the rotting processes. In this case, a corresponding drop in the water level at each waste water inlet is ensured by the drop height between the inlet of the inlet 2 and the water level in the chamber, which is determined by the location of the suction opening of the outlet pipe 6, thereby improving the aeration of the waste water.
Predčistená odpadová voda, zbavená pevných látok, odtekajúca z komory 5 predčisťovacieho a usadzovacieho zariadenia 1, sa dostáva do biologického čistiaceho stupňa 13, opatreného dvoma odvetraniami 14, ktorý bude bližšie objasnený pomocou obr. 3 a 4. Z biologického čistiaceho stupňa 13 sa dostáva vyčistená voda cez odťahovacie potrubie 15, opatrené odvetrávacími nátrubkami 16, do vsakovacej šachty 17, ktorá je rovnako opatrená odvetranímThe purified waste water, free of solids, discharged from the chamber 5 of the pretreatment and settling device 1, enters a biological treatment stage 13 provided with two ventilations 14, which will be explained in more detail with reference to FIG. 3 and 4. From the biological purification stage 13, the purified water enters through the exhaust duct 15 provided with venting sleeves 16, into the infiltration shaft 17, which is also provided with venting
18.18th
Pritom je v oblasti ústia odťahovacieho potrubia 15 usporiadaný filter 19 s aktívnym uhlím.In this case, an activated carbon filter 19 is provided in the region of the mouth of the exhaust pipe 15.
Vsakovacia šachta 17 stojí na asi 40 cm hrubej vrstve 20 praného piesku so zrnitosťou v rozmedzí 30 až 100 mm a má pieskové lôžko 21 s hrúbkou asi 20 cm so zrnitosťou priemeru až do 4 mm. Pieskové lôžko 21 je v oblasti ležiacej pod ústím odťahovacieho potrubia 15 chránené odrazovou doskou 22 vyrobenou z betónu.The infiltration shaft 17 stands on an approximately 40 cm thick layer 20 of washed sand having a grain size of 30 to 100 mm and has a sand bed 21 having a thickness of about 20 cm with a grain size of up to 4 mm. The sand bed 21 is protected by a reflecting plate 22 made of concrete in the area below the mouth of the withdrawal pipe 15.
Ako je možné vidieť z obr. 3, má biologický čistiaci stupeň 13 stenu 23, rozprestierajúcu sa v jeho pozdĺžnom smere, ktorá je opatrená otvormi 24. Táto stena 23 delí oblasť, v ktorej sú usporiadané filtre 25, 26, 27, 28, od oblasti, v ktorej je usporiadané pieskové lôžko 29,30.As can be seen from FIG. 3, the biological cleaning stage 13 has a wall 23 extending in its longitudinal direction which is provided with apertures 24. This wall 23 divides the area in which the filters 25, 26, 27, 28 are arranged from the area in which the sand is arranged bed 29.30.
Ako je možné vidieť z obr. 4, sú filtre 25, 26, 27, 28 na svojej spodnej strane spojené s rúnom 31, 32 z plastu, pričom spodná vrstva 31 rúna najvyššie umiestneného filtra 25 je podstatne hrubšia ako vrstvy 32 rúna zvyšných troch filtrov 26, 27, 28 a má hrúbku asi 9 mm, zatiaľ čo vrstvy 32 rúna majú hrúbku asi 1 mm.As can be seen from FIG. 4, the filters 25, 26, 27, 28 are connected at their underside to the plastic web 31, 32, wherein the bottom web 31 of the uppermost filter 25 is substantially thicker than the web layers 32 of the other three filters 26, 27, 28 and a thickness of about 9 mm, while the webs 32 have a thickness of about 1 mm.
Filtre 25, 26, 27, 28 sú uložené na mrežových roštoch 33, nesených profilmi 33, ktoré sú upevnené na vnútornej strane biologického čistiaceho stupňa 13 a na stene 23.The filters 25, 26, 27, 28 are mounted on gratings 33 supported by profiles 33 which are fixed on the inside of the biological treatment stage 13 and on the wall 23.
Najvyššie umiestnený filter 25 je na svojej hornej strane spojený s ďalšou vrstvou rúna 34 z plastových vlákien. Okrem toho je v oblasti bezprostredne pod ústím odtokovej rúrky 6 usporiadaná odrazová doska 35 vyrobená z betónu.The uppermost filter 25 is connected at its upper side to another layer of plastic fiber web 34. In addition, a reflection plate 35 made of concrete is provided in the area immediately below the mouth of the drain pipe 6.
Pod štyrmi filtrami 25, 26, 27, 28 je usporiadaná betónová vrstva 36, ktorej povrch má sklon, pričom v oblasti najhlbšieho bodu tejto betónovej vrstvy 36 je usporiadaná prietoková rúrka 37, prechádzajúca stenou 23. Tadiaľ sa dostáva vyčistená voda k pieskovému lôžku 29, 30, ktoré je v oblasti ústia prietokovej rúrky 37 chránené odrazovou doskou 38.Below the four filters 25, 26, 27, 28 is arranged a concrete layer 36, the surface of which is inclined, with a flow pipe 37 passing through the wall 23 in the region of the deepest point of the concrete layer 36. 30, which is protected by a reflector plate 38 in the region of the mouth of the flow tube 37.
Čistenie odpadovej vody sa v biologickom čistiacom stupni 13 vykonáva za aeróbnych podmienok, pričom potrebný vzduch je k dispozícii jednak zo vzduchu, prítomného vo filtroch 25, 26, 27, 28 vyrobených z minerálnej alebo sklenenej vlny a jednak vetraním medzipriestorov 39 medzi filtrami pomocou otvorov 24 v stene 23.The wastewater treatment in the biological treatment stage 13 is carried out under aerobic conditions, the necessary air being available both from the air present in the filters 25, 26, 27, 28 made of mineral or glass wool and by venting the interspaces 39 between the filters through the apertures 24 in the wall 23.
Okrem toho dochádza narážaním vody na odrazovú dosku 35 k značnému prevzdušňovaniu vody, takže je k dispozícii dostatok vzduchu na aeróbny proces odbúravania.In addition, by striking water on the baffle plate 35, there is considerable aeration of the water so that sufficient air is available for the aerobic degradation process.
Filtre 25, 26, 27, 28 sa zanášajú začínajúc od oblasti obklopujúcej odrazovú dosku 35 k okrajom filtra, čím sa zmenšuje výška filtrov 25, 26, 27, 28 a vzduch prítomný vo filtroch sa mieša s čistenou vodou.The filters 25, 26, 27, 28 are clogged starting from the area surrounding the reflector plate 35 to the filter edges, thereby reducing the height of the filters 25, 26, 27, 28 and mixing the air present in the filters with purified water.
Ako je zrejmé z obr. 3, je usporiadané navíjacie zariadenie 40, ktoré je z dôvodov lepšej prehľadnosti znázornené iba na obr. 3. Pozostáva v podstate zo štyroch vyberateľné uložených navijakov 41, na ktoré môžu byť použité filtre 25, 26, 27, 28 navinuté. Voda, vytlačená pri navíjaní filtrov, tečie vždy na nižšie sa nachádzajúci filter, prípadne na betónovú vrstvu 36 a pieskové lôžko 29, 30.As shown in FIG. 3, a winding device 40 is provided, which for the sake of clarity is only shown in FIG. 3. It consists essentially of four removably mounted winches 41 to which the filters 25, 26, 27, 28 can be wound. The water displaced by the filter winding always flows onto the lower filter or the concrete layer 36 and the sand bed 29, 30.
Pri výmene filtrov 25, 26, 27, 28 sa môžu použité filtre jednoducho navinúť a vybrať spolu s navijakmi. Po nasadení nových navijakov 41 s navinutými čerstvými filtrami sa filtre z nich vytiahnu a rozprestrú sa na rošte 33.When replacing the filters 25, 26, 27, 28, the used filters can be easily wound up and removed together with the winches. After the new reels 41 have been wound with the fresh filters wound, the filters are pulled out and spread out on the grate 33.
Voda vystupujúca z pieskového lôžka 29, 30 vstupuje do filtra 42 s aktívnym uhlím, ktorý je predradený vstupu odťahovacieho potrubia 15.The water exiting the sand bed 29, 30 enters the activated carbon filter 42 upstream of the inlet duct 15.
Tým sa zaistí, že sa odpadová voda dostane do vsakovacej šachty 17, cez ktorú sa odvádza do okolia, do značnej miery vyčistená.This ensures that the waste water enters the infiltration shaft 17, through which it is discharged into the environment, to a large extent purified.
PATENTOVÉ NÁROKYPATENT CLAIMS
Claims (6)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT0022195U AT670U1 (en) | 1995-04-20 | 1995-04-20 | WASTEWATER PLANT |
PCT/AT1996/000074 WO1996033136A1 (en) | 1995-04-20 | 1996-04-17 | Waste water treatment plant |
Publications (2)
Publication Number | Publication Date |
---|---|
SK141197A3 SK141197A3 (en) | 1998-02-04 |
SK283567B6 true SK283567B6 (en) | 2003-09-11 |
Family
ID=3484757
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SK1411-97A SK283567B6 (en) | 1995-04-20 | 1996-04-17 | Waste water treatment plant |
Country Status (14)
Country | Link |
---|---|
EP (2) | EP0738687A1 (en) |
CN (1) | CN1098814C (en) |
AT (2) | AT670U1 (en) |
AU (1) | AU5260496A (en) |
CZ (1) | CZ290137B6 (en) |
DE (1) | DE59601112D1 (en) |
ES (1) | ES2126395T3 (en) |
HU (1) | HU220021B (en) |
PL (1) | PL183369B1 (en) |
RO (1) | RO117843B1 (en) |
SI (1) | SI0821658T1 (en) |
SK (1) | SK283567B6 (en) |
TR (1) | TR199701187T1 (en) |
WO (1) | WO1996033136A1 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AUPO768897A0 (en) * | 1997-07-02 | 1997-07-24 | Urriola, Humberto | Waste water treatment system |
AT407741B (en) * | 1999-06-04 | 2001-05-25 | Schlatte Anton | Inflow unit in a wastewater treatment plant |
KR20020043737A (en) * | 2000-12-04 | 2002-06-12 | 이찬기 | Trick. Com Process |
FI114859B (en) * | 2003-06-09 | 2005-01-14 | Biolan Oy | Small wastewater treatment plant |
DE102009020202A1 (en) * | 2009-05-07 | 2010-11-11 | Engelhardt, Karl, Dipl.-Ing. (FH) | Small wastewater treatment plant with ring filter |
DE102009027980A1 (en) | 2009-07-23 | 2011-02-03 | Tariq Kaddoura | Wastewater treatment plant and method for treating wastewater and a wastewater treatment system |
SE536403C2 (en) * | 2011-12-15 | 2013-10-08 | Xylem Ip Holdings Llc | Wastewater treatment plant and method for reducing high levels of harmful fluids in wastewater |
AT515820B1 (en) * | 2014-05-15 | 2018-08-15 | Anton Schlatte | Biological purification stage of a sewage treatment plant |
AU2015388682A1 (en) | 2015-03-30 | 2017-11-16 | Ecoglobe Gmbh | Wastewater treatment plant and method for treating wastewater |
CN113548743B (en) * | 2021-08-07 | 2023-11-21 | 湖南省紫鹊界国梁米业有限公司 | Agricultural non-point source pollution treatment equipment |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
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GB1333585A (en) * | 1969-09-12 | 1973-10-10 | Tymoszczuk J | Biological aerated filters |
US3933641A (en) * | 1974-03-04 | 1976-01-20 | Environs Engineering Enterprises, Inc. | Sewage treatment and recycling system |
FR2518523A1 (en) * | 1981-12-17 | 1983-06-24 | Deridder Nicole | Bacterial liquid treatment process - uses multistage impregnated porous beds spaced to allow gas absorption between stages |
AT385750B (en) * | 1985-01-11 | 1988-05-10 | Stoiser & Wolschner | PLANT FOR PURIFYING POLLUTED WATER |
AT391125B (en) * | 1986-05-05 | 1990-08-27 | Stoiser & Wolschner | Arrangement for cleaning up polluted water |
DE3805615A1 (en) * | 1988-02-19 | 1989-08-31 | Mannesmann Ag | Process and apparatus for decreasing the pollutant content of waste water |
AT397381B (en) * | 1991-03-20 | 1994-03-25 | Herbert Dipl Ing Ainedter | BIOLOGICAL WASTE WATER TREATMENT REACTOR |
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1995
- 1995-04-20 AT AT0022195U patent/AT670U1/en not_active IP Right Cessation
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1996
- 1996-03-29 EP EP96890063A patent/EP0738687A1/en not_active Withdrawn
- 1996-04-17 DE DE59601112T patent/DE59601112D1/en not_active Expired - Fee Related
- 1996-04-17 SI SI9630041T patent/SI0821658T1/en not_active IP Right Cessation
- 1996-04-17 AU AU52604/96A patent/AU5260496A/en not_active Abandoned
- 1996-04-17 EP EP96908914A patent/EP0821658B1/en not_active Expired - Lifetime
- 1996-04-17 HU HU9801589A patent/HU220021B/en not_active IP Right Cessation
- 1996-04-17 AT AT96908914T patent/ATE175401T1/en active
- 1996-04-17 WO PCT/AT1996/000074 patent/WO1996033136A1/en active IP Right Grant
- 1996-04-17 ES ES96908914T patent/ES2126395T3/en not_active Expired - Lifetime
- 1996-04-17 CZ CZ19973316A patent/CZ290137B6/en not_active IP Right Cessation
- 1996-04-17 PL PL96322903A patent/PL183369B1/en unknown
- 1996-04-17 RO RO97-01869A patent/RO117843B1/en unknown
- 1996-04-17 SK SK1411-97A patent/SK283567B6/en unknown
- 1996-04-17 TR TR97/01187T patent/TR199701187T1/en unknown
- 1996-04-18 CN CN96105111A patent/CN1098814C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
AU5260496A (en) | 1996-11-07 |
CN1098814C (en) | 2003-01-15 |
HU220021B (en) | 2001-10-28 |
ATE175401T1 (en) | 1999-01-15 |
RO117843B1 (en) | 2002-08-30 |
DE59601112D1 (en) | 1999-02-18 |
PL183369B1 (en) | 2002-06-28 |
EP0821658A1 (en) | 1998-02-04 |
HUP9801589A3 (en) | 1999-01-28 |
TR199701187T1 (en) | 1998-03-21 |
EP0821658B1 (en) | 1999-01-07 |
ES2126395T3 (en) | 1999-03-16 |
CN1139078A (en) | 1997-01-01 |
SK141197A3 (en) | 1998-02-04 |
PL322903A1 (en) | 1998-03-02 |
AT670U1 (en) | 1996-03-25 |
CZ331697A3 (en) | 1998-01-14 |
EP0738687A1 (en) | 1996-10-23 |
WO1996033136A1 (en) | 1996-10-24 |
CZ290137B6 (en) | 2002-06-12 |
HUP9801589A2 (en) | 1998-10-28 |
SI0821658T1 (en) | 1999-04-30 |
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