SK5697Y1 - Device for waste disposal - Google Patents

Device for waste disposal Download PDF

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Publication number
SK5697Y1
SK5697Y1 SK5026-2010U SK50262010U SK5697Y1 SK 5697 Y1 SK5697 Y1 SK 5697Y1 SK 50262010 U SK50262010 U SK 50262010U SK 5697 Y1 SK5697 Y1 SK 5697Y1
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SK
Slovakia
Prior art keywords
tank
sorption
medium
waste disposal
hazardous waste
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Application number
SK5026-2010U
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Slovak (sk)
Other versions
SK50262010U1 (en
Inventor
Jan Ostrica
Original Assignee
Sierra Entpr S R O
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Sierra Entpr S R O filed Critical Sierra Entpr S R O
Priority to SK5026-2010U priority Critical patent/SK5697Y1/en
Publication of SK50262010U1 publication Critical patent/SK50262010U1/en
Publication of SK5697Y1 publication Critical patent/SK5697Y1/en
Priority to CZ201124285U priority patent/CZ22404U1/en
Priority to EEU201100040U priority patent/EE01154U1/en
Priority to HU1100123U priority patent/HU4044U/en
Priority to RS20110026U priority patent/RS1251U/en
Priority to FI20114024U priority patent/FI9395U1/en
Priority to DE201120100486 priority patent/DE202011100486U1/en

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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
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
    • 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
    • B01D17/08—Thickening liquid suspensions by filtration
    • B01D17/10—Thickening liquid suspensions by filtration with stationary filtering elements
    • 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
    • B01D21/0006—Settling tanks provided with means for cleaning and maintenance
    • 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
    • B01D21/003—Sedimentation tanks provided with a plurality of compartments separated by a partition wall
    • 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
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/245—Discharge mechanisms for the sediments
    • B01D21/2483—Means or provisions for manually removing the sediments
    • 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
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
    • 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
    • C02F2101/32—Hydrocarbons, e.g. oil
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal 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)
  • Water Treatment By Sorption (AREA)

Abstract

Described is a device for disposing of hazardous waste consisting of tank (1) equipped on the one hand, has fallen below (11) purified medium and the second deletion (12) purified medium. Tank (1) is divided into technological breakthroughs for at least two workspaces (13), (14), whereby in the first workspace (13) is in the direction of the clean carrier medium located wall (131) and the coalescence filter (132) and the second working space (14) is equipped with at least one sorption filter (141), and continues the cover (17) of tank (1) provided with at least two job openings (171), (172).

Description

SK 5697 Υ1SK 5697-1

Oblasť technikyTechnical field

Technické riešenie sa týka zariadenia na zneškodňovanie nebezpečných odpadov vyskytujúcich sa v tekutej alebo polotekutej forme ako sú odpady z odlučovačov oleja z vody, kaly z odlučovačov oleja, odpady obsahujúce olej, vodné kvapalné odpady s obsahom nebezpečných látok, vodné kvapalné odpady a vodné koncentráty zo sanácie podzemnej vody a podobne najmä kvapalných odpadov s obsahom ropných látok, pričom toto zneškodňovanie sa môže uskutočniť in situ.The technical solution relates to a device for the disposal of hazardous wastes occurring in liquid or semi-liquid form, such as oil separators from water separators, sludges from oil separators, oil-containing wastes, aqueous liquid wastes containing dangerous substances, aqueous liquid wastes and aqueous remediation concentrates groundwater and the like, in particular liquid wastes containing petroleum substances, which disposal may take place in situ.

Doterajší stav technikyBACKGROUND OF THE INVENTION

V oblasti zneškodňovania nebezpečných odpadov definovaných vyššie je známych množstvo riešení, pričom sa používajú rôzne druhy filtrov so sorpčnými materiálmi, ktoré sú regenerovateľné alebo jednorazové, ktoré sa po použití odstraňujú spaľovaním. Väčšina týchto zariadení je veľkorozmerné, čo spôsobuje, že čistené médiá je k týmto potrebné dopravovať na vykonanie čistiacej operácie, pričom do rozhodnutia o začatí čistiacej operácie sú tieto médiá zhromažďované na príslušnom zbernom mieste.A number of solutions are known in the field of hazardous waste disposal as defined above, using various types of filters with sorbent materials that are regenerable or disposable, which are removed by combustion after use. Most of these devices are large-sized, causing the cleaned media to be transported to carry out the cleaning operation, and the media is collected at the appropriate collection point until the decision to start the cleaning operation.

Podstata technického riešeniaThe essence of the technical solution

Teraz sa zistilo, že nevýhody opísaného stavu do značnej miery odstraňuje zariadenie na zneškodňovanie nebezpečných odpadov podľa tohto technického riešenia, ktoré pozostáva z nádrže, vybavenej na jednej strane núteným prívodom čisteného média a na druhej výpustom prečisteného média. Nádrž je technologickými prepážkami rozdelená najmenej na dva, výhodou na tri priestory umožňujúce tri stupne čistenia. Po nútenom prívode čisteného média do prvého priestoru vybavenom v smere toku čisteného média nomou stenou a koalescenčným filtrom a relatívnom ukľudnení toku dochádza v tomto priestore k sedimentácii mechanických nečistôt a čiastočnému odlúčeniu ropných látok, ktoré vyflotované vyplávajú na hladinu. Následne sa čistené médium podrobí čistiacej operácii na koalescenčnom filtri a postupuje do druhého priestoru vybaveného vhodným sorpčným filtrom. Čistené médium sa tu podrobí sorpčnej filtrácii a následne sa ešte prípadne v treťom priestore dočistí filtráciou na aktívnom uhlí a odtokovým potrubím cez kanalizačnú šachtu odvedie do recipientu.It has now been found that the disadvantages of the described state are largely eliminated by the hazardous waste disposal plant according to the present invention, which consists of a tank equipped with a forced supply of purified medium on one side and a purified medium discharge on the other. The tank is divided by technological partitions into at least two, preferably three compartments allowing three stages of cleaning. After the forced supply of the cleaned medium to the first space equipped with a wall and coalescing filter in the direction of the cleaned medium flow and relative calming of the flow, there is a sedimentation of mechanical impurities in this space and partial separation of petroleum substances floated to the surface. Subsequently, the cleaned medium is subjected to a cleaning operation on a coalescing filter and proceeds to a second space equipped with a suitable sorption filter. Here, the purified medium is subjected to sorption filtration and subsequently, if necessary in the third space, it is further purified by filtration on activated carbon and discharged through a sewer shaft to a recipient.

Prípadne sa zachytený nebezpečný odpad odovzdá na ďalšie spracovanie známymi o sebe známymi metódami napríklad biodegradáciou.Alternatively, the recovered hazardous waste is handed over for further treatment by methods known per se, for example by biodegradation.

Je výhodné ak je nádrž pred vstupom čisteného média do prvého priestoru vybavená filtrom na zachytenie najväčších mechanických nečistôt.Advantageously, the tank is equipped with a filter to catch the largest mechanical impurities before the cleaned medium enters the first space.

Horná stena nádrže je vhodne vybavená pracovnými otvormi slúžiacimi na kontrolu technologického procesu a prípadný pracovný zásah.The upper wall of the tank is suitably equipped with working openings to control the technological process and possible work intervention.

Ako sorpčný filter je vhodné použiť komerčné sorpčné filtre, napríklad sorpčné rukávy alebo sorpčné koše.As a sorption filter it is suitable to use commercial sorption filters, for example sorption sleeves or sorption baskets.

Podstatnou výhodou zariadenia je, že vzhľadom na rozmery je možné umiestniť ho na mobilnom podvozku. Táto výhoda umožní zneškodňovanie nebezpečných odpadov v mieste ich vzniku.An essential advantage of the device is that due to its dimensions it can be placed on a mobile chassis. This advantage will allow the disposal of hazardous wastes at the point of generation.

Prehľad obrázkov na výkresochBRIEF DESCRIPTION OF THE DRAWINGS

Technické riešenie bude teraz bližšie znázornené pomocou príkladov a pripojených výkresov, kde na obr. 1 je schematicky znázornený rez nádržou zariadenia na zneškodňovanie nebezpečných odpadov.The technical solution will now be illustrated in more detail with the aid of the examples and the accompanying drawings, in which FIG. 1 is a schematic cross-section through a tank of a hazardous waste disposal plant.

Príklady uskutočnenia technického riešeniaExamples of technical solution

Príklad 1Example 1

Zariadenie podľa technického riešenia bolo použité na zneškodňovanie nepolámych extrahovateľných látok (NEL) z vody v lokalite Dongjin Sebes Gôd - Újtelep ZJ-2 vo výrobnej hale. Analýzou podľa metódy ŠPP ORG-MV-O6 GC typ A sa stanovila miera znečistenia NEL na výšku 2212,306 mg/I a určil sa technologický postup. Rýchlosť prítoku čisteného média bola regulovaná systémom Zariadenie pozostáva z nádrže 1, vybavenej núteným prívodom _H čisteného média a na druhej strane výpustom 12 prečisteného média. Nádrž i je technologickými prekážkami rozdelená na tri pracovné priestory 13,14, 15. V prvom pracovnom priestore je v smere toku čisteného média umiestnená nomá stena 131 a koalescenčný filter 132. Druhý pracovný priestor 14 je vybavený dvojicou sorpčných filtrov 141, 14ľ, ktorými sú sorpčné koše. Kryt 17 nádržeThe device according to the technical solution was used for the disposal of non-breakable extractable substances (NEL) from the water in the locality Dongjin Sebes Gód - Újtelep ZJ-2 in the production hall. Analysis of the SPP ORG-MV-O6 GC type A method determined the NEL contamination rate at 2212.306 mg / L and determined the process. The flow rate of the purified medium was controlled by the system. The apparatus consists of a tank 1 equipped with a forced inlet 11 of the purified medium and, on the other hand, a discharge 12 of the purified medium. The tank 1 is divided into three working spaces 13, 14, 15 by technological obstacles. In the first working space there is a nominal wall 131 and a coalescing filter 132. downstream of the cleaned medium. The second working space 14 is equipped with two sorption filters 141, 14 '. sorption baskets. Tank cover 17

SK 5697 Υ1 je vybavený pracovnými otvormi 171, 172,173, umožňujúcimi kontrolu priebehu čistiaceho procesu ako aj prípadné potrebné vonkajšie zásahy do procesu napríklad výmenu zanesených sorpčných rukávov za nové. V treťom pracovnom priestore 15 je umiestnený filter 151 s aktívnym uhlím.SK 5697 Υ1 is equipped with working openings 171, 172,173, which enable control of the cleaning process as well as possible necessary external interventions in the process, for example replacement of clogged sorption sleeves with new ones. An activated carbon filter 151 is disposed in the third working space 15.

Po nútenom prívode čisteného média do prvého priestoru 13 vybavenom v smere toku čisteného média nomou stenou 131 a koalescenčným filtrom 132 a relatívnom ukľudnení toku dochádza v tomto prvom pracovnom priestore 13 k sedimentácii mechanických nečistôt a čiastočnému odlúčeniu ropných látok, ktoré vyflotované vyplávajú na hladinu. Na nornej stene 131· Následne sa čistené médium podrobí čistiacej operácii na koalescenčnom filtri 132 a postupuje do druhého pracovného priestoru 14 vybaveného dvojicou sorpčných filtrov 141, 141' predstavujúcich sorpčné rukávy. Čistené médium sa tu podrobí sorpčnej filtrácii a následne sa v treťom pracovnom priestore 15 dočisťuje filtráciou na aktívnom uhlí a výpustom 12 a odtokovým potrubím cez kanalizačnú šachtu odvedie do recipientu. Zariadenie bolo umiestnené na špeciálne upravenom podvozku.After the forced supply of the cleaned medium to the first chamber 13 provided with a downstream wall 131 and a coalescing filter 132 in the direction of the cleaned medium flow and relative flow soothing, the first workspace 13 causes sedimentation of mechanical impurities and partial separation of petroleum substances floating. Subsequently, the cleaned medium is subjected to a cleaning operation on a coalescing filter 132 and proceeds to a second working space 14 equipped with a pair of sorption filters 141, 141 'representing sorption sleeves. Here, the purified medium is subjected to sorption filtration and is subsequently cleaned in the third working space 15 by filtration on activated carbon and by discharge 12 and discharged via a sewer shaft to a recipient. The device was placed on a specially modified chassis.

Hodnoty znečistenia NEL na výstupe z mobilného zariadenia na zneškodňovanie odpadov boli stanovené metódou ŠPP ORG-MV-06 GC typ A na výšku 0,420 mg/1.The NEL pollution values at the outlet of the mobile waste disposal facility were determined by the SPG ORG-MV-06 GC type A method at 0.420 mg / l.

Príklad 2Example 2

Na zariadení podľa technického riešenia sa čistila zaolejovaná voda v lokalite Dongjin Sebes Gód - Ujtelep ZJ-2 vo výrobnej hale. Analýzou podľa metódy ŠPP ORG-MV-06 GC typ A sa stanovila miera znečistenia NEL na výšku 2212,306 mg/1 a určil sa technologický postup. Rýchlosť prítoku čisteného média bola regulovaná systémom. Zariadenie pozostávalo z nádrže 1, vybavenej núteným prívodom H čisteného média a na druhej strane výpustom 12 prečisteného média. Nádrž 1 je technologickými prekážkami rozdelená na tri pracovné priestory 13. 14.15, V prvom pracovnom priestore je v smere toku čisteného média umiestnená nomá stena 131 a koalescenčný filter 132. Druhý pracovný priestor 14 je vybavený dvojicou sorpčných filtrov 141, 141’, ktorými sú sorpčné rukávy. Kryt nádrže je vybavený pracovnými otvormi 171, 172 umožňujúcimi kontrolu priebehu čistiaceho procesu ako aj prípadné potrebné vonkajšie zásahy do procesu napríklad výmenu zanesených sorpčných rukávov za nové. V treťom pracovnom priestore 15 je umiestnený filter 151 s aktívnym uhlím.The equipment according to the technical solution was cleaned with oily water at Dongjin Sebes Gód - Ujtelep ZJ-2 in the production hall. Analysis by SPP ORG-MV-06 GC Type A method determined the NEL pollution level at 2212.306 mg / L and determined the process. The flow rate of the purified medium was controlled by the system. The apparatus consisted of a tank 1, equipped with a forced supply of purified medium H and, on the other hand, with a discharge 12 of purified medium. The tank 1 is divided into three working spaces 13 by technological obstacles. sleeves. The tank cover is equipped with working openings 171, 172 for monitoring the cleaning process as well as any necessary external interventions in the process, for example, replacing clogged sorption sleeves with new ones. An activated carbon filter 151 is disposed in the third working space 15.

Po nútenom prívode čisteného média do prvého priestoru 13 vybavenom v smere toku čisteného média nornou stenou 131 a koalescenčným filtrom 132 a relatívnom ukľudnení toku dochádza v tomto prvom pracovnom priestore k sedimentácii mechanických nečistôt a čiastočnému odlúčeniu ropných látok, ktoré vyflotované vyplávajú na hladinu. Na nornej stene 131. Následne sa čistené médium podrobí čistiacej operácii na koalescenčnom filtri 132 a postupuje do druhého pracovného priestoru 14 vybaveného dvojicou sorpčných filtrov 141, 141' predstavujúcich sorpčné rukávy. Čistené médium sa tu podrobí sorpčnej filtrácii a následne sa v treťom pracovnom priestore 15 dočisťuje filtráciou na aktívnom uhlí a výpustom 12 a odtokovým potrubím cez kanalizačnú šachtu odvedie do recipientu. Zariadenie bolo umiestnené na špeciálne upravenom podvozku. V tomto prípade nebolo použité dočisťovanie filtráciou na aktívnom uhlí.After the forced supply of the purified medium to the first space 13 equipped with a normal wall 131 and a coalescing filter 132 in the direction of the flow of the purified medium and relative flow soothing, mechanical impurities are sedimented and partially separated in the first working space. On the normal wall 131. Subsequently, the cleaned medium is subjected to a cleaning operation on a coalescing filter 132 and proceeds to a second working space 14 equipped with a pair of sorption filters 141, 141 'representing sorption sleeves. Here, the purified medium is subjected to sorption filtration and is subsequently cleaned in the third working space 15 by filtration on activated carbon and by discharge 12 and discharged via a sewer shaft to a recipient. The device was placed on a specially modified chassis. In this case, the post-treatment with activated carbon was not used.

Hodnoty znečistenia NEL na výstupe z mobilného zariadenia na zneškodňovanie odpadov boli stanovené metódou ŠPP ORG-MV-06 GC typ A na výšku 4,754 mg/1.The NEL pollution values at the outlet of the mobile waste disposal facility were determined using the SPG ORG-MV-06 GC type A method at 4.754 mg / l.

Priemyselná využiteľnosťIndustrial usability

Ako preukazujú uvedené konkrétne príklady použitia má zariadenie podľa technického riešenia široké využitie pri zneškodňovaní nebezpečných odpadov na základe vysokej účinnosti a mobility zariadenia umožňujúcej mu pracovať in situ.As shown by the specific examples of use, the device according to the invention has a wide application in the disposal of hazardous waste on the basis of the high efficiency and mobility of the device enabling it to work in situ.

NÁROKY NA OCHRANUPROTECTION REQUIREMENTS

Claims (5)

1. Zariadenie na zneškodňovanie nebezpečných odpadov, vyznačujúce sa tým, že pozostáva z nádrže (1) vybavenej na jednej strane núteným prívodom (11) čisteného média a na druhej výpustom (12) prečisteného média a nádrž (1) je technologickými prepážkami rozdelená najmenej na dva pracovné priestory (13, 14), pričom v prvom pracovnom priestore (13) je v smere postupu čisteného média umiestnená nomá stena (131) a koalescenčný filter (132) a druhý pracovný priestor (14) je vybavený najmenej jedným sorpčným filtrom (141) pričom ďalej je kryt (17) nádrže (1) vybavený najmenej dvomi pracovnými otvormi (171,172).Hazardous waste disposal plant, characterized in that it consists of a tank (1) equipped on one side with a forced supply (11) of purified medium and on the other side (12) of purified medium and the tank (1) is divided into at least two working spaces (13, 14), wherein a first wall (131) and a coalescing filter (132) are located in the first working space (13) downstream of the cleaned medium and the second working space (14) is equipped with at least one sorption filter (141) ) wherein the cover (17) of the tank (1) is provided with at least two working openings (171, 172). 2. Zariadenie na zneškodňovanie nebezpečných odpadov podľa nároku 1, vyznačujúce sa tým, že v nádrži (1) je v smere toku čisteného média vytvorený tretí pracovný priestor (15) vybavený filtrom (151) s aktívnym uhlím.Hazardous waste disposal device according to claim 1, characterized in that a third working space (15) equipped with an activated carbon filter (151) is formed in the tank (1) downstream of the cleaned medium. SK 5697 Υ1SK 5697-1 3. Zariadenie na zneškodňovanie nebezpečných odpadov podľa nároku 1 alebo 2, vyznačujúce sa tým, že prvý priestor (13) nádrže (1) je na prívode (11) čisteného média vybavený filtrom mechanických nečistôt.Hazardous waste disposal device according to claim 1 or 2, characterized in that the first chamber (13) of the tank (1) is equipped with a mechanical impurity filter at the inlet (11) of the cleaned medium. 4. Zariadenie na zneškodňovanie nebezpečných odpadov podľa nároku 1 alebo 2, vyznačujúce 5 sa tým, že v druhom pracovnom priestore (14) sa ako sorpčné filtre (141, 141') používajú sorpčné rukávy alebo sorpčné koše.Hazardous waste disposal device according to claim 1 or 2, characterized in that sorption sleeves or sorption baskets are used as sorption filters (141, 141 ') in the second working space (14). 5. Zariadenie na zneškodňovanie nebezpečných odpadov podľa ktoréhokoľvek z predchádzajúcich nárokov, vyznačujúce sa tým, že je umiestnené na mobilnom podvozku.Hazardous waste disposal device according to any one of the preceding claims, characterized in that it is located on a mobile chassis.
SK5026-2010U 2010-05-07 2010-05-07 Device for waste disposal SK5697Y1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
SK5026-2010U SK5697Y1 (en) 2010-05-07 2010-05-07 Device for waste disposal
CZ201124285U CZ22404U1 (en) 2010-05-07 2011-05-03 Waste disposal apparatus
EEU201100040U EE01154U1 (en) 2010-05-07 2011-05-04 Device for dealing with hazardous waste
HU1100123U HU4044U (en) 2010-05-07 2011-05-04 Waste disposal device
RS20110026U RS1251U (en) 2010-05-07 2011-05-06 Device for a hazardous waste treatment
FI20114024U FI9395U1 (en) 2010-05-07 2011-05-06 Waste Removal Device
DE201120100486 DE202011100486U1 (en) 2010-05-07 2011-05-09 Waste disposal facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SK5026-2010U SK5697Y1 (en) 2010-05-07 2010-05-07 Device for waste disposal

Publications (2)

Publication Number Publication Date
SK50262010U1 SK50262010U1 (en) 2010-09-07
SK5697Y1 true SK5697Y1 (en) 2011-03-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
SK5026-2010U SK5697Y1 (en) 2010-05-07 2010-05-07 Device for waste disposal

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CZ (1) CZ22404U1 (en)
DE (1) DE202011100486U1 (en)
EE (1) EE01154U1 (en)
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CN104649452A (en) * 2015-02-15 2015-05-27 上海大众祥源动力供应有限公司 Slag bath system capable of blocking scummings
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