HRP20180511T1 - Postupak i uređaj za obradu tekućeg mulja i filtarski kolači dobiveni ovim postupkom - Google Patents
Postupak i uređaj za obradu tekućeg mulja i filtarski kolači dobiveni ovim postupkom Download PDFInfo
- Publication number
- HRP20180511T1 HRP20180511T1 HRP20180511TT HRP20180511T HRP20180511T1 HR P20180511 T1 HRP20180511 T1 HR P20180511T1 HR P20180511T T HRP20180511T T HR P20180511TT HR P20180511 T HRP20180511 T HR P20180511T HR P20180511 T1 HRP20180511 T1 HR P20180511T1
- Authority
- HR
- Croatia
- Prior art keywords
- tank
- liquid sludge
- air
- emulsion
- sludge
- Prior art date
Links
- 239000010802 sludge Substances 0.000 title claims 30
- 239000007788 liquid Substances 0.000 title claims 27
- 238000000034 method Methods 0.000 title claims 25
- 239000012065 filter cake Substances 0.000 title claims 2
- 239000000839 emulsion Substances 0.000 claims 15
- 239000003153 chemical reaction reagent Substances 0.000 claims 8
- 239000000725 suspension Substances 0.000 claims 7
- 238000001914 filtration Methods 0.000 claims 4
- 238000013022 venting Methods 0.000 claims 4
- 238000002347 injection Methods 0.000 claims 3
- 239000007924 injection Substances 0.000 claims 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims 2
- 235000011941 Tilia x europaea Nutrition 0.000 claims 2
- 230000015271 coagulation Effects 0.000 claims 2
- 238000005345 coagulation Methods 0.000 claims 2
- 238000007872 degassing Methods 0.000 claims 2
- 238000005188 flotation Methods 0.000 claims 2
- 239000004571 lime Substances 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 2
- 230000003647 oxidation Effects 0.000 claims 2
- 238000007254 oxidation reaction Methods 0.000 claims 2
- 238000005192 partition Methods 0.000 claims 2
- 229940088417 precipitated calcium carbonate Drugs 0.000 claims 2
- 230000001737 promoting effect Effects 0.000 claims 2
- 239000004576 sand Substances 0.000 claims 2
- 230000003068 static effect Effects 0.000 claims 2
- 238000011144 upstream manufacturing Methods 0.000 claims 2
- 238000005119 centrifugation Methods 0.000 claims 1
- 238000010908 decantation Methods 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 claims 1
- 238000011049 filling Methods 0.000 claims 1
- 229920000642 polymer Polymers 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
Classifications
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- B01D21/0084—Enhancing liquid-particle separation using the flotation principle
-
- 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
- B01D21/02—Settling tanks with single outlets for the separated liquid
- B01D21/08—Settling tanks with single outlets for the separated liquid provided with flocculating compartments
-
- 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
- B01D21/2494—Feed or discharge mechanisms for settling tanks provided with means for the removal of gas, e.g. noxious gas, air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/214—Mixing gases with liquids by introducing liquids into gaseous media using a gas-liquid mixing column or tower
-
- 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
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- 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
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- 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
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
- C02F11/147—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents using organic substances
-
- 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
- B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/25—Mixing by jets impinging against collision plates
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
-
- 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
- C02F2209/38—Gas flow rate
-
- 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
- C02F2209/40—Liquid flow rate
-
- 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
- C02F2301/06—Pressure conditions
- C02F2301/066—Overpressure, high pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Claims (35)
1. Postupak za obradu i preradu tekućeg mulja (2, 31), pri čemu se prva emulzija mulja (14, 57, 89) stvara u povezanoj posudi pod pritiskom (5, 6, 33, 52, 83, 117, 119, 131) u koju se kontinuirano dovodi tekući mulj s prvom brzinom protoka Q (m3/h), sudaranjem tekućeg mulja (2, 31, 81) sa zrakom (13) koji se ubrizgava u spremnik (5) brzinom protoka Q' (Nm3/h), pri čemu je Q' > 5Q, pražnjenje navedene prve emulzije odvija se na izlazu spremnika preko komponenti (18, 38, 61) koje stvaraju gubitak tlaka, zatim se filtriranje ili dekantiranje tako dobivene suspendirane tvari emulzije (23) provodi odvajanjem od tekuće frakcije (27, 49, 105, 112) koja se prazni kontinuirano, naznačen time, da se za stvaranje navedene prve emulzije sudaranjem mulja sa zrakom, mulj (2) i zrak (13) injektiraju u prvu zonu (8, 56, 84, 117, 133) posude, a tako formirana emulzija odvodi se prema drugoj zoni (16, 59, 91, 119, 141) spremnika koja se proteže preko prve zadane duljine L1, injektiranje zraka i guste otopine u prvu zonu i duljina L1 pridonose stvaranju prve emulzije koja se sastoji od kapljica mulja u zraku, potom se provodi pražnjenje prve emulzije iz spremnika, preko komponente koja stvara gubitak tlaka u cjevastom kućištu (19, 43, 62, 121) koje se proteže duž druge zadane duljine L2, u koju se ubrizgava barem jedan flokulant (22, 45, 73, 98, 123), kako bi se u navedenom kućištu dobila druga emulzija zraka u koaguliranom i flokuliranom tekućem mulju, te da je navedena druga emulzija (20, 46, 67) barem djelomično otplinjena odzračivanjem (20) kućišta prije navedene filtracije (25, 25') ili dekantiranja.
2. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da prva zona ima mali volumen koji je manji od 0,05 m3.
3. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je prva zadana duljina L1 veća od 50 cm.
4. Postupak u skladu s patentnim zahtjevom 3, naznačen time, da je druga zadana duljina L2 veća od 1 m.
5. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je srednji tlak P u spremniku (5, 33) takav da je 1,5 bar <P <10 bara i Q' takav da je 10 Q ≤ Q' ≤ 100 Q.
6. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je emulzija uglavnom otplinjena na izlazu spremnika, u unutrašnjosti komore za otplinjavanje (95, 124) opremljene sredstvima za miješanje (96).
7. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je povezani spremnik (8) kolona (6) prosječnog promjera d i visine H ≥ 10 d, a tekući mulj (2) se uvodi u donji dio (10) kolone u plinovitom sloju koji je stvoren zrakom koji se ubrizgava na razini navedenog punjenja mulja.
8. Postupak u skladu s patentnim zahtjevom 7, naznačen time, da se tekući mulj (2) u koloni (6) raspršuje na unutarnju stijenku (11) ili na pregradu spremnika kako bi se poboljšala njezino raspadanje u plinovitom toku.
9. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se suspenzija (2) uvodi u donji dio (10) posude (5, 6) preko statičkog miksera.
10. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je flokulant (22, 45, 73) polimer koji se ubrizgava u neposredni izlaz posude, prije odzračivanja.
11. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se najmanje jedan reagens koji je odabran između pijeska, kalcijevog karbonata, istaloženog vapna, reagensa za oksidaciju i / ili reagensa za promicanje koagulacije, uvodi uzvodno od spremnika (6) u tok tekućeg mulja.
12. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se najmanje jedan reagens odabran između pijeska, kalcijevog karbonata, istaloženog vapna, reagensa za oksidaciju i / ili reagensa za promicanje koagulacije, uvodi nizvodno od spremnika.
13. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da je kućište (19, 62, 94) cjevasto i ima prosječni presjek protoka jednak presjeku spremnika.
14. Postupak u skladu s patentnim zahtjevom 13, naznačen time, da kućište sadržava najmanje jedan element (18, 61, 97) koji stvara gubitak tlaka iza izlaza posude (6, 52), na čijem se izlazu se ubrizgava flokulant.
15. Postupak u skladu s patentnim zahtjevom 14, naznačen time, da kućište sadržava barem još jedan element koji stvara gubitak tlaka prije prvog elementa, na izlazu kojeg se uvodi najmanje jedan reagens i / ili zrak.
16. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da su element ili elementi koji stvaraju gubitak tlaka Venturi cijevi (18, 38, 44, 64).
17. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se brzo i / ili uglavnom trenutačno provodi koncentriranje tekućeg mulja flotacijom / taloženjem flokulirane emulzije u volumenu (101, 128, 166, 180) koji djeluje kao koncentrator.
18. Postupak u skladu s patentnim zahtjevom 17, naznačen time, da se suspenzija uklanja prelijevanjem iz koncentratora.
19. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se obrada tekućeg mulja nizvodno od cjevastog kućišta provodi centrifugiranjem, filtracijom i / ili pritiskom.
20. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se injektirani zrak zagrijava i / ili miješa s parom.
21. Postupak u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time, da se zrak ubrizgava na način da formira spiralni protok u toku tekućeg mulja.
22. Uređaj za obradu i preradu tekućeg mulja koji sadržava povezani spremnik (5, 6, 33, 52, 83, 117, 119, 131), sredstva (3, 82) za kontinuiranu opskrbu spomenutog spremnika tekućim muljem (2, 31) pri prvoj brzini protoka Q (m3/h), sredstva (87) za napajanje spomenutog spremnika zrakom pri brzini protoka Q' (Nm3/h), gdje Q' ≥ 5Q i sredstva (25, 25', 68) za filtriranje i / ili dekantiranje emulzije koja se tako flokulira, raspoređena tako da odvaja tekuću frakciju suspendirane tvari i neprekidno je vraća u proces, naznačen time, da su sredstva (3, 82) za punjenje spremnika tekućim muljem i zrakom postavljena tako da se tekući mulj i zrak injektiraju u prvu zonu posude, zatim se prenose duž prve duljine L1, da bi se stvorila prva emulzija kapljica tekućeg mulja u zraku, i s time da obuhvaća kućište (19, 39, 62, 93, 121) za uklanjanje prve emulzije koja je dobivena u spremniku preko komponente (18, 38, 61) koja uzrokuje gubitak tlaka, kućište (19, 39, 62) je cjevastog oblika i proteže se preko zadane duljine L2 i obuhvaća sredstva za odzračivanje i sredstva (21, 72, 98, 123) za ubrizgavanje barem jednog flokulanta (22, 45, 73) u navedeno cjevasto kućište u odnosu na navedeno odzračivanje, tako da tvori drugu emulziju zraka u koaguliranom i flokuliranom tekućem mulju.
23. Uređaj u skladu s patentnim zahtjevom 22, naznačen time, da prva zona spremnika ima mali volumen manji od 0,05 m3 koji je omeđen između dviju stijenki protoka.
24. Uređaj u skladu s bilo kojim od patentnih zahtjeva 22 i 23, naznačen time, da je povezani spremnik (5, 33, 52) kolona (6) prosječnog promjera d i visine H ≥ 10 d, a tekući mulj uvodi se u donji dio (10) kolone u plinovitom sloju kojeg stvara ubrizgavanje zraka na razini navedenog ulaza tekući mulj.
25. Uređaj u skladu s patentnim zahtjevom 24, naznačen time, da kolona (6) nadalje sadržava unutarnju pregradu postavljenu na izlazu sredstva za ubrizgavanje u kolonu, radi razbijanja mlaza tekućeg mulja.
26. Uređaj u skladu s bilo kojim od patentnih zahtjeva 22 do 25, naznačen time, da obuhvaća statički mikser za tekući mulj uzvodno od spremnika.
27. Uređaj u skladu s bilo kojim od patentnih zahtjeva 22 do 26, naznačen time, da je kućište (19, 62, 94) cijevno s prosječnim presjekom protoka koji je ekvivalentan onom u spremniku.
28. Uređaj u skladu s patentnim zahtjevom 27, naznačen time, da cjevasto kućište (16) obuhvaća barem jedan element (18, 44, 61, 97) koji stvara gubitak tlaka nizvodno od izlaza spremnika, na izlazu na kojem se ubrizgava flokulant.
29. Uređaj u skladu s patentnim zahtjevom 28, naznačen time, da cjevasto kućište sadržava najmanje još jedan element (38) koji stvara gubitak tlaka prije prvog elementa, na čijem se izlazu uvodi najmanje jedan reagens i / ili zrak (42).
30. Uređaj prema bilo kojem zahtjevu 28 i 29, naznačen time, da su element ili elementi koji stvaraju gubitak tlaka Venturi cijevi.
31. Uređaj u skladu s bilo kojim od prethodnih patentnih zahtjeva 22 do 30, naznačen time, da nadalje sadržava komoru za otplinjavanje (95, 124) nizvodno od spremnika koji je opremljen sredstvima za miješanje (96).
32. Uređaj u skladu s jednim od patentnih zahtjeva 22 do 31, naznačen time, da nadalje sadržava volumen (101, 128, 166, 180) nizvodno od kućišta koji djeluje kao koncentrator postavljen tako da omogućava flotaciju flokulirane suspenzije tekućeg mulja na zadanoj visini.
33. Uređaj u skladu s patentnim zahtjevom 32, naznačen time, da volumen obuhvaća sredstva (107, 159, 160, 173, 174) za uklanjanje suspenzije prelijevanjem.
34. Skrutnuti (filtarski) kolač suspenzije organskog tekućeg mulja dobiven postupkom u skladu s bilo kojim od patentnih zahtjeva 1 do 21, naznačen time, da je dobiven iz organske suspenzije tekućeg mulja i da ima gustoću između 0,5 i 0,9 g/cm3.
35. Filtarski kolač organske suspenzije tekućeg mulja u skladu s patentnim zahtjevom 34, naznačen time, da ima poroznost od 85 % ± 5%.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR1361706A FR3013702A1 (fr) | 2013-11-27 | 2013-11-27 | Procede et dispositif de traitement de boues liquides, et galettes de boues obtenues avec un tel procede. |
| FR1302857A FR3013700B1 (fr) | 2013-11-27 | 2013-12-06 | Procede et dispositif de traitement de boues liquides, et galettes de boues obtenues avec un tel procede |
| EP14814976.8A EP3094393B8 (fr) | 2013-11-27 | 2014-11-27 | Procede et dispositif de traitement de boues liquides, et galettes de boues obtenues avec un tel procede |
| PCT/FR2014/053063 WO2015079175A1 (fr) | 2013-11-27 | 2014-11-27 | Procede et dispositif de traitement de boues liquides, et galettes de boues obtenues avec un tel procede |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HRP20180511T1 true HRP20180511T1 (hr) | 2018-05-04 |
Family
ID=50473405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HRP20180511TT HRP20180511T1 (hr) | 2013-11-27 | 2018-03-27 | Postupak i uređaj za obradu tekućeg mulja i filtarski kolači dobiveni ovim postupkom |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US10919783B2 (hr) |
| AR (1) | AR100299A1 (hr) |
| DK (1) | DK3094393T3 (hr) |
| EA (1) | EA038733B1 (hr) |
| ES (1) | ES2664760T3 (hr) |
| FR (2) | FR3013702A1 (hr) |
| HK (1) | HK1226020B (hr) |
| HR (1) | HRP20180511T1 (hr) |
| HU (1) | HUE038628T2 (hr) |
| MA (1) | MA39052B1 (hr) |
| MX (1) | MX2016006681A (hr) |
| NO (1) | NO3094393T3 (hr) |
| PH (1) | PH12016500990A1 (hr) |
| PT (1) | PT3094393T (hr) |
| TN (1) | TN2016000190A1 (hr) |
| ZA (1) | ZA201603589B (hr) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108179774B (zh) * | 2018-02-07 | 2023-09-26 | 广州市昊力工具有限公司 | 淤泥输送系统及清淤干泥船 |
| FR3081860B1 (fr) * | 2018-06-01 | 2022-07-08 | Orege | Procede et dispositif de traitement pour deshydratation de boues organiques |
| FR3091277B1 (fr) * | 2018-12-26 | 2021-07-23 | Orege | Procédé et dispositif d’amélioration de la biodégradabilité d’une boue |
| FR3091276B1 (fr) * | 2018-12-26 | 2021-06-18 | Orege | Procédé et dispositif de méthanisation améliorés |
| CN115849649B (zh) * | 2023-03-01 | 2023-05-26 | 广东省科学院生态环境与土壤研究所 | 一种高压喷射污泥减容装置 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT392062B (de) * | 1987-12-28 | 1991-01-25 | Herbert Pfefferkorn | Verfahren zum eindicken von abwasserschlaemmen und/oder anderen organischen schlaemmen sowie einrichtung zur durchfuehrung dieses verfahrens |
| US4869829A (en) * | 1988-06-29 | 1989-09-26 | Nalco Chemical Company | Process for separating solids with a keratin filter aid |
| WO2008024755A1 (en) * | 2006-08-24 | 2008-02-28 | Morse Dwain E | Control system and process for wastewater treatment |
| DE102006054156A1 (de) * | 2006-11-16 | 2008-05-21 | Wacker Chemie Ag | Pyrogene Kieselsäure hergestellt in einer Produktions-Anlage mit großer Kapazität |
| FR2966818B1 (fr) * | 2010-10-29 | 2014-02-14 | Orege | Procede de separation entre liquide et matiere en suspension d'une boue et dispositif mettant en oeuvre un tel procede. |
-
2013
- 2013-11-27 FR FR1361706A patent/FR3013702A1/fr active Pending
- 2013-12-06 FR FR1302857A patent/FR3013700B1/fr not_active Expired - Fee Related
-
2014
- 2014-11-26 AR ARP140104424A patent/AR100299A1/es unknown
- 2014-11-27 NO NO14814976A patent/NO3094393T3/no unknown
- 2014-11-27 HU HUE14814976A patent/HUE038628T2/hu unknown
- 2014-11-27 MX MX2016006681A patent/MX2016006681A/es unknown
- 2014-11-27 PT PT148149768T patent/PT3094393T/pt unknown
- 2014-11-27 TN TN2016000190A patent/TN2016000190A1/fr unknown
- 2014-11-27 EA EA201600353A patent/EA038733B1/ru unknown
- 2014-11-27 ES ES14814976.8T patent/ES2664760T3/es active Active
- 2014-11-27 DK DK14814976.8T patent/DK3094393T3/en active
- 2014-11-27 US US15/039,812 patent/US10919783B2/en active Active
- 2014-11-27 MA MA39052A patent/MA39052B1/fr unknown
-
2016
- 2016-05-25 ZA ZA2016/03589A patent/ZA201603589B/en unknown
- 2016-05-26 PH PH12016500990A patent/PH12016500990A1/en unknown
- 2016-12-22 HK HK16114602A patent/HK1226020B/zh unknown
-
2018
- 2018-03-27 HR HRP20180511TT patent/HRP20180511T1/hr unknown
Also Published As
| Publication number | Publication date |
|---|---|
| EA038733B1 (ru) | 2021-10-12 |
| FR3013700B1 (fr) | 2017-03-24 |
| US20170029291A1 (en) | 2017-02-02 |
| HUE038628T2 (hu) | 2018-11-28 |
| TN2016000190A1 (fr) | 2017-10-06 |
| US10919783B2 (en) | 2021-02-16 |
| ZA201603589B (en) | 2017-11-29 |
| HK1226020B (zh) | 2017-09-22 |
| MA39052A1 (fr) | 2017-02-28 |
| PT3094393T (pt) | 2018-04-06 |
| MA39052B1 (fr) | 2017-10-31 |
| ES2664760T3 (es) | 2018-04-23 |
| FR3013700A1 (fr) | 2015-05-29 |
| EA201600353A1 (ru) | 2017-04-28 |
| MX2016006681A (es) | 2017-01-16 |
| PH12016500990A1 (en) | 2016-06-20 |
| FR3013702A1 (fr) | 2015-05-29 |
| DK3094393T3 (en) | 2018-04-23 |
| AR100299A1 (es) | 2016-09-28 |
| NO3094393T3 (hr) | 2018-06-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| HRP20180511T1 (hr) | Postupak i uređaj za obradu tekućeg mulja i filtarski kolači dobiveni ovim postupkom | |
| JP2016538125A5 (hr) | ||
| US10518274B2 (en) | Flocculation basin inclusion or exclusion type water treatment apparatus using dissolved air flotation | |
| JP6495909B2 (ja) | 液体スラッジを処理する方法及び装置ならびに当該方法によって得られるフィルターケーキ | |
| KR100919367B1 (ko) | 고효율 기체용해탱크를 이용한 부상분리장치 | |
| KR101336169B1 (ko) | 침전과 부상을 연계한 고도정수처리장치 | |
| KR101602289B1 (ko) | 역 와류형 미세기포 발생장치를 이용한 가압부상설비 | |
| JP2016087564A5 (hr) | ||
| RU143767U1 (ru) | Установка для комплексной очистки питьевой воды | |
| SE535787C2 (sv) | Vattenrenare och metod för att rena vatten | |
| CN107635633B (zh) | 从液体汽提气体的脱气装置和方法 | |
| JP6580338B2 (ja) | 膜処理装置及び膜処理方法 | |
| KR101743642B1 (ko) | 기포 발생기를 포함하는 수처리장치 | |
| IL274592B2 (en) | Plant and method for treating municipal waste water | |
| JP2009240911A (ja) | 散気装置及び散気装置を備えた膜濃縮装置を有する水処理施設 | |
| JP6164941B2 (ja) | 濁水処理システムおよび濁水処理方法 | |
| KR101694919B1 (ko) | 무동력 혼화응집조 및 이를 포함하는 용존공기부상장치 | |
| RU162450U1 (ru) | Сатуратор | |
| CN208218448U (zh) | 一种喷涂废水气浮处理设备 | |
| RU2019111286A (ru) | Способ и устройство для прямого извлечения ценных минералов в виде агрегатов, состоящих из пузырьков и твердых частиц | |
| RU2524601C1 (ru) | Установка безреагентной очистки и обеззараживания воды | |
| KR20170038452A (ko) | 복합형 가압부상 여과처리 장치 | |
| KR102110508B1 (ko) | 유기물 회수량을 증가시킬 수 있는 용존공기부상 장치 및 이를 이용하는 수처리 방법 | |
| CN108996770A (zh) | 一种快速高效除油气浮滤池 | |
| JP2015134328A (ja) | フッ素含有溶液からのフッ素化合物除去方法 |