SK87491A3 - Separator of light liquids - Google Patents
Separator of light liquids Download PDFInfo
- Publication number
- SK87491A3 SK87491A3 SK874-91A SK87491A SK87491A3 SK 87491 A3 SK87491 A3 SK 87491A3 SK 87491 A SK87491 A SK 87491A SK 87491 A3 SK87491 A3 SK 87491A3
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- separator
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- 239000007788 liquid Substances 0.000 title claims description 19
- 230000015271 coagulation Effects 0.000 claims description 7
- 238000005345 coagulation Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims 1
- 230000008878 coupling Effects 0.000 claims 1
- 238000010168 coupling process Methods 0.000 claims 1
- 238000005859 coupling reaction Methods 0.000 claims 1
- 230000001419 dependent effect Effects 0.000 claims 1
- 229910052740 iodine Inorganic materials 0.000 claims 1
- 239000011630 iodine Substances 0.000 claims 1
- 230000002068 genetic effect Effects 0.000 abstract 4
- 230000011218 segmentation Effects 0.000 abstract 3
- 230000006978 adaptation Effects 0.000 abstract 1
- 230000003044 adaptive effect Effects 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000003709 image segmentation Methods 0.000 abstract 1
- 230000000977 initiatory effect Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 210000002966 serum Anatomy 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/307—Passive control mechanisms without external energy, e.g. using a float
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
- B01D17/0211—Separation of non-miscible liquids by sedimentation with baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/045—Breaking emulsions with coalescers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0012—Settling tanks making use of filters, e.g. by floating layers of particulate material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0048—Plurality of plates inclined in alternating directions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/34—Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
-
- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03F—SEWERS; CESSPOOLS
- E03F5/00—Sewerage structures
- E03F5/14—Devices for separating liquid or solid substances from sewage, e.g. sand or sludge traps, rakes or grates
- E03F5/16—Devices for separating oil, water or grease from sewage in drains leading to the main sewer
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Public Health (AREA)
- Water Supply & Treatment (AREA)
- Removal Of Floating Material (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
Vynález se týká odlučovače pro lehké kapaliny, u ktorého se ve hrubém odlučovači odlučuj! odsadítelné usazenlny a v alespoň jednom dále zarazeném jemném odlučovači se odlučuj! naplavované lehké kapaliny, pŕičeaž hrubý odlučovač je opatren vestavbami, pomoci ktorých se lehké kapaliny odlučuj! již ve hrubém odlučovači.The present invention relates to a separator for light liquids in which they are separated in a coarse separator. separable settlements and in at least one downstream fine separator are separated! alluvial light liquids, the coarse separator being equipped with built-in units, by means of which the light liquids are separated! already in the coarse separator.
Dosavadní stav technikyBACKGROUND OF THE INVENTION
Když probíhá také u známýoh zaŕízení Již ve hrubém odlučovači dílen! vyplavávající lehké kapaliny, potom je toto dílen! tak nepatrné, že je poslední odlučovač v proudu odpadni vody pomerní vyeoce zatížován, takže je potrebné časté čistín! tohoto posledního odlučovače. Toto e sebou pŕináíí dlouhé čekaoí doby.When it also takes place with known systems Already in the rough workshop separator! leaching light liquids, then this workshop! so small that the last separator in the waste water stream is relatively heavily loaded, so frequent cleaning is required! this last separator. This brings long waiting times.
Podstata vynálezu 'Jkolem predloženého vynálezu je zkonstruován! odlučovače, ktorý by nevykazoval výše uvedené nevýhody, a u ktorého by byly proto náklady na čištíní nižší.SUMMARY OF THE INVENTION The object of the present invention is constructed. a separator which does not exhibit the above disadvantages and for which the cleaning costs would therefore be lower.
Uvedeného oíle se dosáhne podie predloženého vynálezu jednoduchým zpúeobem tak, že se za jemný odlučovač zaradí odlučovač zbytkových olejú, praoující na koaleecenčním princípu, a že rovnéž v jeinném odlučovači je uspoŕádán koalescenční filtr.According to the present invention, this object is achieved in a simple manner by providing a fine separator with a residual oil separator flowing on the co-equivalence principle, and that a coalescing filter is also provided in the other separator.
V celkové» čistíoím ŕetčzci tím část čiôténí preložená dopredu a tím se odlehčí část nej citlivé j $í na pre— tíšení, totiž odlučovač zbytkových olejú· Výhodné je koalesoenční filtr v jemném odlučovači uspoŕádán pod nahromadénou vrstvou lehké k a paliny. Takto se ne.-u'že ucpat olejem.In the overall purification chain, the part of the fabrics folded forward and thereby relieving the part most sensitive to overloading, namely the residual oil separator. Preferably, the coalescing filter in the fine separator is arranged below the accumulated layer of light metal and wood. In this way, it cannot clog with oil.
Kromé toho je koalesoenční filtr výhodné ohránén proti primárnu nábéhu odrazovým plechom, který současné pŕebírá fyzikálni procesy čistení adsorpcí, a tím odlehčuje koalesoenčnímu filtru.In addition, the coalescing filter is advantageously bent against the primary run-in by a reflector plate, which at the same time takes over the physical processes of adsorption purification and thereby relieves the coalescing filter.
Jako koalescenční filtry jsou použitelné souproudé a protiproudé filtry, pričemž u souproudého filtru probíhá prfttok vody a oddélované lehké kapaliny v jednom eméru a u protiproudého filtru v opačné» sméru. Výhoda souproudého filtru epočívá v podpororání odlučovacího účinku a v nopatrném filtrační» odporu | nevýhodné je znečistení na neprístupné spodní strane filtru. Výhodné u protiproudého filtru je znočiéténí pouze na lehoe prístupné horní strané filtru a silnéjší koalescenční účinok prodloužením cesty a arovnáním kapiček. Nevýhodné je však nebezpečí splachování do výtoku.Current and countercurrent filters can be used as coalescing filters, with a flow of water and separated light liquids flowing in one emerge and a countercurrent filter in the opposite direction. The advantage of a co-current filter lies in the support of the separating effect and in a slight filter resistance »» | a disadvantage is contamination on the inaccessible bottom of the filter. Advantageously, in a countercurrent filter, it is imbibed only on the readily accessible top side of the filter and the stronger coalescing effect by extending the path and leveling the droplets. However, the danger of flushing into the outlet is disadvantageous.
Ďalším o í lom predloženého vynálezu je sjednooení výhod souproudých a protiproudých filtrú bez toho. Že by ee pŕevzaly jejich nevýhody. Toho se dosáhne tím, že koaleecenční filtr v odlučovači zbytkových olejú je v podstaté schopný nábéhu ze čtyŕ straň ve sméru od výtokové trubky. Tím so zahučtuje ve s.iéru k odtoku zrnční granulátu a klade se prítoku podstatný odpor. Vzájemným trením granulátu se formují vétéí částice, ktoré buä stoupají /lehké kapaliny/ nebo klesají /olejové kaly/. Prosto nedochází k žádným usazeninám znočišténin na voIné ze všeoh straň pŕístupném filtru a neočekává se také žádné ucpávání uBazeninami, nebol usadeniny klesaj í smerom dolú a povrch filtru zúatává voIný.A further object of the present invention is to unify the advantages of co-current and counter-current filters without this. That they would assume their disadvantages. This is achieved by the fact that the coalescing filter in the residual oil separator is substantially capable of starting up in four directions in the direction away from the outlet pipe. As a result, the granulate granules are thickened in the serum and a substantial resistance is introduced. By friction of the granulate, larger particles are formed which either rise (light liquids) or fall (oil sludges). There is simply no soiling of the pollutants on the freely accessible filter and no clogging is also expected, the deposits are not downward and the surface of the filter is free.
Pomoci opatrení podie predloženého vynálezu je také možné po odčorpání objemu vody čištční zafízoní tlakovou vodou bez toho, že by a· filtr musel vy j inou t. Tím mohou také odpadnout vaechna proplaohovací zaŕízení, která jsou nutná u souproudých i protiproudých filtrú.By means of the measures of the present invention, it is also possible, after the volume of water has been drained, to purify the pressurized water without the filter having to do otherwise. This can also eliminate all the back-up devices required for both upstream and downstream filters.
Aby se zaŕízení podie predloženého vynálezu chránilo pred koneentrečníml nárazy a zahlcením, je podie dalžího znaku vynálezu p?ed nátokem do hrubého odlučovače uspofádán prítokový regulátor, rízený plovákem a mSnící prô.rez prítoku v závislosti na výňce hladiny kapaliny·In order to protect the device according to the present invention from concetration impacts and flooding, according to another feature of the invention, a flow regulator controlled by a float and a flow cross section depending on the liquid level rise are arranged before the inlet into the coarse separator.
Aby se doeáhlo turbulentního proudéní, podporuj ίο í ho klesaní usazenin, je podie dalsího znaku predloženého vynálezu usporádán jako veatavba ve hrubém odlučovači mezi nátokem a výtokom koagulační filtr· Tento múže být tvoŕen podlouhlými profily, smérujíoími smžrom dolú, ktoré jsou uložený otočné a/nebo poaouvateln'~ tak, aby byl nastaviteľný odstup mezi nimi·According to a further feature of the present invention, a coagulation filter is provided in the rough separator between the inlet and the outlet, in order to achieve turbulent flow, to promote the descent of the deposits. adjustable so that the distance between them is adjustable ·
Délka uvedených profilú se zvčteuje ve siéru od výtoku, usarený kal naohází tedy odpovídající místo.The length of the profiles is increased in the serum from the outlet, so the boiled sludge casts a corresponding place.
Objasnení obrázkú na výkresoch / náeledujídím je predložený vynález blíže popsán pomoci príkladu provedení, znázornených na obrazeích, bez toho, že by se omezoval pouze ne tyto príklady.BRIEF DESCRIPTION OF THE DRAWINGS The present invention will be described in more detail with reference to the exemplary embodiments shown in the drawings, without being limited thereto.
Obr. 1 znázorňuje schematicky v púdorysu odlučovač podlo vynálezu , obr. 2 predstavuje rez v rovine II-II podie obr. 1 , obr. 3 a 4 znázorňují schematicky v nárysu a pôdorysu uepo*ádání koagulačního filtru a zFig. 1 shows schematically in a plan view a separator according to the invention, FIG. 2 is a section along II-II in FIG. 1, FIG. 3 and 4 show schematically, in front and top view, the arrangement of the coagulation filter and
obr. 5 a 6 usporádání j Iného koagulačriího filtru.Fig. 5 and 6 of another coagulation filter arrangement.
Podie obrázkú seetává odlučovač pro lehké kapaliny ze hrubého odlučovače 1 , jemného odlučovače £ a odlučovače J zbytkovýcb olej’i. *iľt?ní :.lpalní voda prochází preš nátok J do hrubého odlučovače JL a opouätí jej ponorenou trubkou ^38 · Nátok J leží u tohoto príkladu provedení pod hladinou J kaoaliny, určenou prepadom £ do jemného odlučovače 2 a je opatren aŕítokovýn regulátorem B , ovládaným plovákein. Tento prítokový ptai regulátor 8 seetává v podstaté z listu Soupátka 10 , pripevneného na plováku Jg , ktorý v závislosti na stavu kapaliny otevírá nebo pŕivírá prdŕez nátoku · iAccording to the figures, a separator for light liquids from the coarse separator 1, the fine separator 8 and the residual oil separator J are set up. The water inlet passes through the inlet J into the coarse separator JL and leaves it through a submerged pipe. In this example, the inlet J lies below the level J of the kaloaline determined by the overflow 6 into the fine separator 2 and is provided with a flow regulator B. controlled float. The inflow feeder regulator 8 essentially consists of a sheet of the Stem 10 mounted on a float 11 which, depending on the liquid state, opens or closes the inlet of the inlet.
ňrubý odlučovač 1 je vybaven velkoryse vynoreným kalovým proetorem 14 * ve kterém se odsazují usazeniny 15 . Z dôvodu zabudování ponorené trubky se väak odlučuj í nejen usazeniny 15 nýbrž také vyplavávající lehké kapaliny 16 · Jak pokusy ukázaly, mohou být v heiibém odlučovači .1 odloučeny velké části odlučovaných lehkých kapalin.The coarse separator 1 is equipped with a generously emitted sludge proetor 14 * in which deposits 15 are deposited. However, due to the incorporation of the submerged pipe, not only deposits 15 but also leaching light liquids 16 are separated. As has been shown, large parts of the light liquids to be separated can be separated in the heel separator.
Prítok 17 jemného odlučovače 2 je opatfen uzá/érem 16 , regulovaným pomoci plováku, který je o sobé známy. Takovýto uzávčr zavre pri preclení dané m nahromadéní lehkých kapalln samostatné prítok 17 , nádrži Je.iného odlučovače 2 je unísten koar lescenční filtr 19 * který je podie znázorneného príkladu uapofádán jako protiproudý filtr· Odlučování lehkých kapalin se tímto uspoŕádáním podstatné zlepší.The inflow 17 of the fine separator 2 is provided with a lock 16 controlled by a float known per se. Such a closure closes a separate inlet 17 upon clearing of the light liquid accumulation, the coarse filter 19 is mounted in the reservoir of another separator 2. This filter is designed as a countercurrent filter according to the example shown.
J ľoalescenční filtr 19 je pomoci trmenu 19** lehce vyménitelný a je uspoŕádán tak, že také pri nej vyšším stavu olejové vrstvy /uzavrení samostatného uzávéru/ neleží v oblasti olejové vrstvy a nemôže být tedy ucpáván olejem. Kromš toho je tento filtr ohránšn proti pŕímému nábéhu pomoci odrazového plechu 19 , ktorý současné pŕebírá fyzikálni procesy čiätení pomoci adeorpce, a tím odlehčuje koalescenčnímu filtru 19 ·The oil filter 19 is easily replaceable by means of the yoke 19 ** and is arranged such that even at its higher state the oil layer (closing of the separate cap) does not lie in the region of the oil layer and thus cannot be clogged with oil. In addition, the filter is protected against direct start-up by a reflector plate 19, which at the same time takes over the physical processes of adeorption cleaning, thereby relieving the coalescing filter 19.
Od koalescenčního filtru 19 odchází odpadni voda, která je již polstatne zbavena lehkých kapalin, vedením 20 do odlučovače J zbytkovéh··' oleje. ,r tomto je usporádán koalescenČní filtr 21 , který Je protékán ze čtyŕ straň ve sieru k výtokov·? trubce 22 · ’-ί λ ae 'záhušíuje ve smšru k odtoku zrnéní grsnulátu a klade se prôtoku podstatný odpor. Výhodou tohoto shlukování dohromady je samočistící efekt. Vzájomným trenia granulátu se totiž fonnují vštší častice, které buä stoupají /lehké kapaliny/ , nebo se usazují /olejové kaly/.Waste water, which is already substantially free of light liquids, flows from the coalescing filter 19 through line 20 to the residual oil separator. , a coalescence filter 21 is provided which flows from four sides in the sulfur to the outflows? The tube 22 " -ί λ and e " The advantage of this aggregation together is the self-cleaning effect. In fact, the particles of the granulate form larger particles which either rise (light liquids) or settle (oil sludges).
Pomoci uspoMdání podie predloženého vynálezu se obzvlášté ulehčí koalescenčnímu filtru odlučobače 2 ^bytkového oleje a není také tedy treba jej opatrovať zvláštním proplachovacím zaŕízením.With the arrangement according to the present invention, the coalescing filter of the oil separator 2 is particularly facilitated and therefore it is not necessary to provide it with a separate flushing device.
Podie obr. 3 a 4 jsou j ako vestavby ve hrubém odlučovači 1 usporádány podlouhlé, smšrem dolô sméŕujíoí profily 23 , umístčné iczi nátokera J & ponorenou trubkou £ odtoku. Tyto profily 23 jsou otočné a pouvné zavéšeny na ko lej nie ich 24 tak, že je možno s nimi pohybovať ve sméru šlpek, znázornených na obr. 4 . Délka profilô 23 se zvétčuje ve cixru k norené trubce odtoku.According to FIG. 3 and 4, the elongated, downwardly directed profiles 23, which are located in the coarse separator 1, are arranged in the coarse separator 1, positioned in the inlet pipe 6 by the submerged outlet pipe. These profiles 23 are pivotable and hinged to the rail 24 so that they can be moved in the direction of the legs shown in FIG. 4. Profile length is 23 zvétčuje in C ru x to Nora drain pipe.
Profily 23 tvorí samočistící koagulační člen pro jemné kaly. Slouží pro získání lineárni turbulence proudéní a prispívaj í tím ke koagulačnímu efektu. Jemné kaly v dôsledku uspoŕádání teehto profilô se lehoe usazují.The profiles 23 form a self-cleaning coagulation member for fine sludge. They serve to obtain linear flow turbulence and thus contribute to the coagulation effect. Fine sludge due to the arrangement of these profiles settles easily.
•J príkladu provedení oodle obr. 5 a 6 je jako ves tavba ve hrubém odlučovači 1 uiísten koagulační filtr 25 , sestávající ze stupňovité za sebou a vedie sebe uspoŕádaných ohnutých plech·' · ’yto plechy jsou umístčny v komoíe 27 1 která je ve sučru k nátoku 4 zakryte pomoci odelo ňovacího plechu 28 , takže je prichásející odpadni voda rozdvojována, urazí delší cestu a zlepšuje se úČinnost odeazování. L'átok J je opčt opatren prítokovým regulátorom 8 ( ovládaným plovákem £ , Na hrubý odlučovač navazuje stojné jako u príkladu podie obr· 1 a 2 jemný odlučovač· opatrený koalesoenčním filtrera ti odlučovač zbytkového oleje, opatrený koalesoenčním filtreu.FIG. 5 and 6, a coagulation filter 25 is provided as a melt in the coarse separator 1, consisting of a step-by-step sequence and guided by bent sheets arranged one after the other. Thus, the incoming waste water is bifurcated, travels a longer way and improves the de-oiling efficiency. L'Átok opčt J is provided with the inlet 8 a controller (controlled by a float £, for coarse separator is connected is standing in the example of Figures 1 and 2 · fine separator · koalesoenčním Filtrer provided with the separator of the residual oil provided koalesoenčním filtreu.
ráuci vynálezu jsou ak re-.pľ’íklad jednotlivé odlučovače nenusejí být v oddelených stavebních částeoh. Pále je možné umístit >ro jednotlivé odlučovače oddelené komory vo společné stavbe. rlaké je mož né pri obzvlúStních požadavcích na čistotu vyčiňtčné vody zaradit ra odlučovač zhytkových olej$ sdsorpční filtr. Pred hrubý odlučovač 1 je možno zaradít také jeSté dalSí hrubý odlučovač.The invention is an object of the present invention and, for example, individual separators do not have to be in separate building parts. It is also possible to place individual separators of a separate chamber in a common building. R Lake the possible pairs of obzvlúStních purity requirements vyčiňtčné water separator to classify trans zhytkových $ sdsorpční oil filter. A coarse separator 1 may also be provided upstream of the coarse separator 1.
Claims (3)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT0074890A AT394355B (en) | 1990-03-30 | 1990-03-30 | SEPARATOR FOR LIGHTING LIQUIDS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SK87491A3 true SK87491A3 (en) | 1996-04-03 |
Family
ID=3498770
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SK874-91A SK87491A3 (en) | 1990-03-30 | 1991-03-29 | Separator of light liquids |
Country Status (8)
| Country | Link |
|---|---|
| AT (1) | AT394355B (en) |
| CH (1) | CH683002A5 (en) |
| CZ (1) | CZ87491A3 (en) |
| DE (1) | DE4110091A1 (en) |
| HU (1) | HU209659B (en) |
| IT (1) | IT1245608B (en) |
| SK (1) | SK87491A3 (en) |
| YU (1) | YU53591A (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4130812A1 (en) * | 1991-09-17 | 1993-03-18 | Benkeser Michael | LIQUID SEPARATOR |
| AT398752B (en) * | 1992-07-27 | 1995-01-25 | Purator Umwelttechnik Gmbh | SEPARATORS FOR LIQUIDS |
| AT398959B (en) * | 1992-08-27 | 1995-02-27 | Katzenberger Beton U Fertigtei | PLANT FOR SEPARATING LIQUIDS, IN PART. MINERAL OILS |
| DE9308652U1 (en) * | 1992-11-17 | 1993-10-07 | Kessel, Bernhard, 85101 Lenting | Separation plant |
| AT399862B (en) * | 1993-10-05 | 1995-08-25 | Ortner Bauwaren | EXHAUST DEVICE FOR INSTALLATION IN A LIGHT LIQUID SEPARATOR |
| DE19837670A1 (en) * | 1998-08-20 | 2000-02-24 | Michael Benkeser | Separator unit to remove oil, petrol and grease from water has two identical separation basins arranged in sequence improving process efficiency |
| DE10244743B4 (en) * | 2002-09-25 | 2008-09-11 | Aco Severin Ahlmann Gmbh & Co. Kg | Separator system for separating a lighter phase from a wastewater |
| DE102004029326B4 (en) * | 2004-06-10 | 2010-09-16 | Mahle International Gmbh | Process and device for cleaning oily and solids-laden wastewaters |
| US7314549B2 (en) * | 2006-04-14 | 2008-01-01 | Storm Pal Inc. | Storm water interceptor |
| DE102006026632A1 (en) * | 2006-06-08 | 2007-12-13 | Kolb, Frank R., Dr. Ing. | Introducer for reservoir |
| CN107492092A (en) * | 2017-07-13 | 2017-12-19 | 青岛黄海学院 | The medical image cutting method of GSA algorithms is improved based on FCM algorithm fusions |
| US11964221B2 (en) | 2019-11-25 | 2024-04-23 | OSI Environmental, LLC. | Overload protection chamber for fluid separation apparatus and system |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2577917B1 (en) * | 1985-02-26 | 1991-04-26 | Saint Dizier Ste Cale | HYDROCARBON SEPARATOR HYDROFILTER WITH ASSOCIATED COALESCING FILTER |
| DE3612288A1 (en) * | 1986-04-11 | 1987-10-15 | Iwan Koslow | Oil separator |
| DE3731031A1 (en) * | 1987-09-16 | 1989-03-30 | Buderus Bau & Abwassertechnik | Separator for light liquid |
-
1990
- 1990-03-30 AT AT0074890A patent/AT394355B/en not_active IP Right Cessation
-
1991
- 1991-03-25 CH CH901/91A patent/CH683002A5/en not_active IP Right Cessation
- 1991-03-26 YU YU53591A patent/YU53591A/en unknown
- 1991-03-27 DE DE4110091A patent/DE4110091A1/en not_active Withdrawn
- 1991-03-29 HU HU911041A patent/HU209659B/en not_active IP Right Cessation
- 1991-03-29 CZ CS91874A patent/CZ87491A3/en unknown
- 1991-03-29 SK SK874-91A patent/SK87491A3/en unknown
- 1991-03-29 IT ITMI910895A patent/IT1245608B/en active IP Right Grant
Also Published As
| Publication number | Publication date |
|---|---|
| ATA74890A (en) | 1991-09-15 |
| HU209659B (en) | 1994-10-28 |
| ITMI910895A0 (en) | 1991-03-29 |
| CH683002A5 (en) | 1993-12-31 |
| YU53591A (en) | 1994-05-10 |
| DE4110091A1 (en) | 1991-11-21 |
| HU911041D0 (en) | 1991-10-28 |
| IT1245608B (en) | 1994-09-29 |
| ITMI910895A1 (en) | 1992-09-29 |
| CZ87491A3 (en) | 1995-01-18 |
| HUT60642A (en) | 1992-10-28 |
| AT394355B (en) | 1992-03-25 |
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