PL104587B1 - MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS - Google Patents
MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS Download PDFInfo
- Publication number
- PL104587B1 PL104587B1 PL1976188312A PL18831276A PL104587B1 PL 104587 B1 PL104587 B1 PL 104587B1 PL 1976188312 A PL1976188312 A PL 1976188312A PL 18831276 A PL18831276 A PL 18831276A PL 104587 B1 PL104587 B1 PL 104587B1
- Authority
- PL
- Poland
- Prior art keywords
- hydromechanical
- flocked
- mulls
- machine
- mechanical processing
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/48—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D33/50—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/06—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
- B01D33/11—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for outward flow filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Centrifugal Separators (AREA)
Description
Opis patentowy opublikowano: 30.04.1980 104587 Int. Cl1. B01D33/0 B03D 3/06 "CZV iLLNIA Twórcy wynalazku: Zygmunt Skimina, Zbigniew Koszman, Ludwik Spyra, StanislawFrysz, Jerzy Peteja, Jerzy Szczypa, Jaroslaw Neczaj-Hruzewicz, Ryszard Sprycha, Wladyslaw Janusz Uprawniony z patentu: Kopalnia Wegla Kamiennego „Boleslaw Smialy", Laziska Górne; Uniwersytet im. Marii Curie Sklodowskiej, Lublin (Polska) Urzadzenie do ciaglego odwadniania w procesie hydromechanicznej ' i mechanicznej obróbki sflokuIcwanych mulów Wynalazek dotyczy urzadzenia do ciaglego odwadniania w procesie hydromechanicznej i mechanicznej obróbki sflokulowanych mulów.The patent description was published: April 30, 1980 104587 Int. Cl1. B01D33 / 0 B03D 3/06 "CZV iLLNIA Creators of the invention: Zygmunt Skimina, Zbigniew Koszman, Ludwik Spyra, Stanislaw Frysz, Jerzy Peteja, Jerzy Szczypa, Jaroslaw Neczaj-Hruzewicz, Ryszard Sprycha, Wladyslaw Janusz The holder of the patent: "Boleslaw Smialy" Coal Mine, Laziska Górne; University of Maria Curie Sklodowskiej, Lublin (Poland) Continuous dewatering device in a hydromechanical process and mechanical processing of flocked mules The invention relates to a device for continuous dewatering in a hydromechanical and mechanical process treatment of flocculated mules.
Znane jest z praktyki i literatury (Stanislaw Blaschke „Przeróbka mechaniczna kopalin"- Dzial X str. 398-418, Wydawnictwo Slask, Katowice 1972 r. „Poradnik Górnika" TomIV, Wydawnictwo Górni¬ czo-Hutnicze, Katowice 1960 r.) stosowanie do tego celu filtrów prózniowych, przesiewaczy, wirówek i pras.It is known from practice and literature (Stanislaw Blaschke "Mechanical processing of minerals" - Section X pp. 398-418, Wydawnictwo Slask, Katowice 1972. "Poradnik Górnika" TomIV, Wydawnictwo Górni¬ czo-Hutnicze, Katowice 1960) using vacuum filters, screens, centrifuges and presses for this purpose.
Filtry prózniowe charakteryzuja sie niska wydajnoscia i wymagaja udzialu energochlonnych urzadzen towarzy¬ szacych. Ich stosowanie jest ograniczone ponadto do mulów o wskazniku Dahlstroma ponizej 300. Przesiewacze sa równiez malo wydajne, a odprowadzana woda zawiera pokazna ilosc czesci stalych. Wirówki nie zapewniaja mozliwosci uzyskiwania glebokiego odwadniania, a prasy z uwagi na brak ciaglosci pracy równiez sa malo wydajne i uciazliwe w stosowaniu.Vacuum filters are characterized by low efficiency and require the participation of energy-consuming devices accompanying sighs. Their use is further restricted to mussels with a Dahlstrom index below 300. Sifters They are also inefficient and the drainage water contains a good amount of solids. Centrifuges do not provide the possibility of obtaining deep drainage, and the presses, due to the lack of work continuity, are also efficient and cumbersome to use.
Lepsze efekty przy mniejszych nakladach uzyskuje sie stosujac aglomeracje sferyczna sflokulowanych osadów wedlug sposobu znanego miedzy innymi z opisu patentowego PRL nr 87479. Sposób ten polega na dodawaniu do zawiesiny odpowiedniego flokulatora, aglomerowaniu osadów i oddzielaniu powstalych aglomera¬ tów od fazy wodnej. Do stosowania tego sposobu moga byc uzywane rózne urzadzenia, które jednak zawsze musza posiadac elementy wprowadzajace sflokulowany osad w ruch obrotowy, np. obracajacy sie cylindryczny pojemnik, elementy aglomerujace w rodzaju progów na wewnetrznej czesci cylindra (lub slimak, które jedno¬ czesnie transportuja sflokulowany osad do urzadzenia oddzielajacego aglomerat od fazy wodnej np. do sit wibra¬ cyjnych.Better results with lower inputs are obtained when using spherical flocculated agglomerations sludge according to the method known, inter alia, from the patent description of the Polish People's Republic No. 87479. This method consists in adding a suitable flocculator to the slurry, agglomerating the sediments and separating the formed agglomerates from the water phase. Different devices can be used for this method, but always they must have elements that introduce the flocculated sediment into a rotary motion, e.g. a rotating cylindrical one container, agglomerating elements such as thresholds on the inner part of the cylinder (or a screw, which at the same time, they transport the flocculated sludge to a device separating the agglomerate from the water phase, e.g. to vibration screens of
Zasadnicza niedogodnoscia wymienionych urzadzen niezaleznie od ich konstrukcji jest koniecznosc przeno¬ szenia sflokulowanych i zaglomerowanych osadów do urzadzen oddzielajacych faze wodna przez co zmniejsza sie zwiezlosc aglomeratu i wydajnosc calego procesu, oraz nie zawsze osiaga sie glebokie odwodnienie. Dodatkowa niedogodnoscia jest zbyteczna rozbudowa urzadzen do odwadniania.The main disadvantage of the above-mentioned devices, regardless of their design, is the necessity to transport sludge flocculated and agglomerated sludge to devices separating the water phase, which reduces compactness of the agglomerate and efficiency of the entire process, and deep drainage is not always achieved. Additional the inconvenience is the unnecessary expansion of the drainage facilities.
Celem wynalazku jest usuniecie tych niedogodnosci, czyli zwiekszenie wydajnosci oraz uzyskanie produktu stalego o niskiej zawartosci wody, zwiezlosci wystarczajacej do transportu przenosnikami przy równoczesnym2 104587 uzyciu malej ilosci niskiej jakosci flokulanta i odzysku czystej wody, która moze byc zwracana do obiegu cieczy macierzystej. The aim of the invention is to overcome these drawbacks, i.e. to increase the yield and obtain the product solid with a low water content, firmness sufficient for transport by conveyors at the same time2 104587 using a small amount of low quality flocculant and recovering clean water that can be returned to the liquid circuit home.
Zgodnie z wytyczonym zadaniem ciagle odwadnianie sflokulowanych mulów dla otrzymania produktu stalego uzyskuje sie wedlug wynalazku dzieki temu, ze sflokulowane muly wprowadza sie do zamknietego od dolu, nachylonego, obrotowego cylindra o sciankach sitowych, którego wewnetrzna powierzchnie wyposazono w progi równolegle do jego osi, intensyfikujace proces mieszania oraz slimak transportujacy muly do górnego wylotu cylindra, z którego w postaci bezksztaltnej masy zsypuja sie na przenosnik. W procesie transportu slima¬ kiem, mieszanina ulega separacji na klarowna wode wyciekajaca przez otwory sita i bezksztaltna mase stopniowo zgeszczajaca sie. Wielkosc otworów sita obrotowego cylindra uzalezniona jest od wielkosci tworzacych sie granul dla uniemozliwienia przechodzenia ich na zewnatrz, przy równoczesnym stalym odbiorze wody.According to the assigned task, continuously draining the flocculated silts to obtain the product according to the invention, the flocculated mud is introduced into the closed bottom, an inclined, rotating tube with mesh walls, the internal surface of which is equipped with into the thresholds parallel to its axis, intensifying the mixing process and the screw transporting the mules to the upper one cylinder outlet, from which they pour into the conveyor in the form of a shapeless mass. In the process of transporting slime the mixture is separated into clear water leaking through the sieve holes and shapeless mass gradually wheezing. The size of the holes of the cylinder rotary sieve depends on the size of the formed granules to prevent them from passing outside, while at the same time constantly receiving the water.
Korzystnie dla procesu odwadniania jest, gdy wielkosc otworów sita zwieksza sie w miare wzrostu formo¬ wanych w urzadzeniu granul i stopnia odsaczania wody. W górnej czesci cylindra zabudowane sa przylegajace do zewnetrznej jego powierzchni dysze nadmuchu sprezonego powietrza czyszczacego sito co uintensywnia proces odwadniania. Splyw wody do pojemnika, z którego kierowana jest do obiegu cieczy macierzystej, wymuszony zostaje przez kolnierz umieszczony na obwodzie obrotowego cylindra od strony wlotu mieszaniny. Ilosc obro¬ tów i nachylenie cylindra zalezne jest od ilosci odwadnianych mulów.It is advantageous for the dewatering process that the size of the openings of the screen increases as the form grows the granules important in the device and the degree of water extraction. In the upper part of the cylinder, adjacent to the to its surface, compressed air blowing nozzles to clean the sieve, which intensifies the process drainage. Forced drainage of water into the container from which it is directed to the circulation of the mother liquid is placed by a flange on the circumference of the rotating cylinder on the inlet side of the mixture. Number of rotations tilt and cylinder inclination depends on the amount of drained silts.
Przedmiot wynalazku jest uwidoczniony w przykladzie wykonania na rysunku, na którym fig. 1 przedsta¬ wia urzadzenia odwadniajace w widoku z boku, fig. 2 — przekrój podluzny cylindra odwadniacza, a fig. 3 — prze¬ krój poprzeczny cylindra.The subject matter of the invention is illustrated in an exemplary embodiment in the drawing in which Fig. 1 shows side view of the dewatering device, Fig. 2 is a longitudinal section of the dehydrator cylinder, and Fig. 3 is a cross section of cross cylinder cut.
Jak uwidoczniono na fig. 1 i 2 sflokulowana mieszanina doprowadzana jest przewodem rurowym 1 po¬ laczonym centrycznie z dnem 2 obrotowego wykonanego z sita cylindra 3 wyposazonego na? wewnetrznej po¬ wierzchni w progi przewalowe 4 dla procesu mechanicznego formowania granul i slimak 5 transportujacy te granule w kierunku wylotu cylindra. Od strony wlotu mieszaniny na cylindrze zabudowany jest kolnierz 6 wymuszajacy wplyw wody do pojemnika 7. Do górnej czesci cylindra przylegaja dysze 8 nadmuchu sprezonego powietrza czyszczacego sito. Odwodniony w trakcie transportu slimakiem mul wysypuje sie w postaci produktu stalego na przenosnik 9.As shown in FIGS. 1 and 2, the flocculated mixture is fed through the pipeline 1 to connected centrally with the bottom of the 2 rotating cylinder 3 made of sieve, equipped with internal compartment top with rollers 4 for the mechanical shaping process of granules and a screw 5 for transporting these granules towards the exit of the cylinder. On the side of the mixture inlet, a flange 6 is installed on the cylinder forcing water to flow into the container 7. Nozzles 8 for a compressed air blast are attached to the upper part of the cylinder sieve cleaning air. The mule, dehydrated during transport, is poured out in the form of a product fixed on the conveyor 9.
Claims (1)
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL1976188312A PL104587B1 (en) | 1976-03-27 | 1976-03-27 | MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS |
DE2711528A DE2711528C3 (en) | 1976-03-27 | 1977-03-16 | Device for continuous dewatering of flocculated sludge |
GB12579/77A GB1569475A (en) | 1976-03-27 | 1977-03-25 | Apparatus for continuous dewatering in the process of hydromechanical and mechanical treatmentof flocculated sludges |
FR7709071A FR2345197A1 (en) | 1976-03-27 | 1977-03-25 | DEVICE FOR CONTINUOUS DRAINING DURING WET AND MECHANICAL TREATMENT OF FLOCCULATED SCHLAMMS |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL1976188312A PL104587B1 (en) | 1976-03-27 | 1976-03-27 | MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS |
Publications (1)
Publication Number | Publication Date |
---|---|
PL104587B1 true PL104587B1 (en) | 1979-08-31 |
Family
ID=19976173
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PL1976188312A PL104587B1 (en) | 1976-03-27 | 1976-03-27 | MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE2711528C3 (en) |
FR (1) | FR2345197A1 (en) |
GB (1) | GB1569475A (en) |
PL (1) | PL104587B1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4507202A (en) * | 1982-01-18 | 1985-03-26 | Dan Nord | Device for the separation of a liquid |
EP0120039A1 (en) * | 1982-09-29 | 1984-10-03 | Ilecard Pty. Limited | Recovery of solids from dispersions |
CH663357A5 (en) * | 1985-07-11 | 1987-12-15 | Lujari Instmsto Oy | Apparatus for separating solid constituents from waste water |
GB8622875D0 (en) * | 1986-09-23 | 1986-10-29 | Mitchell Cotts Mining Equipmen | Screen assembly |
AT394995B (en) * | 1990-11-08 | 1992-08-10 | Lindner Wolfgang Ing | Apparatus for separating off and compressing solids |
GB2312382A (en) * | 1996-04-23 | 1997-10-29 | Ecological Products Ltd | Sludge thickening apparatus |
CN114772898B (en) * | 2022-05-17 | 2023-06-30 | 浙江华东工程建设管理有限公司 | Simple flocculation dewatering device |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1461453A1 (en) * | 1965-08-20 | 1969-08-07 | Passavant Werke | Thickener for liquids containing solids |
SE346068B (en) * | 1969-04-24 | 1972-06-26 | Ingenioers Fa Vvs Utrustning A |
-
1976
- 1976-03-27 PL PL1976188312A patent/PL104587B1/en unknown
-
1977
- 1977-03-16 DE DE2711528A patent/DE2711528C3/en not_active Expired
- 1977-03-25 FR FR7709071A patent/FR2345197A1/en active Granted
- 1977-03-25 GB GB12579/77A patent/GB1569475A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE2711528C3 (en) | 1981-08-06 |
FR2345197B1 (en) | 1982-01-08 |
FR2345197A1 (en) | 1977-10-21 |
GB1569475A (en) | 1980-06-18 |
DE2711528B2 (en) | 1980-12-18 |
DE2711528A1 (en) | 1977-10-06 |
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