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 PDF

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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
Application number
PL1976188312A
Other languages
Polish (pl)
Original Assignee
Kopalnia Wegla Kamiennego Bolesl
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.)
Filing date
Publication date
Application filed by Kopalnia Wegla Kamiennego Bolesl filed Critical Kopalnia Wegla Kamiennego Bolesl
Priority to PL1976188312A priority Critical patent/PL104587B1/en
Priority to DE2711528A priority patent/DE2711528C3/en
Priority to GB12579/77A priority patent/GB1569475A/en
Priority to FR7709071A priority patent/FR2345197A1/en
Publication of PL104587B1 publication Critical patent/PL104587B1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/44Regenerating the filter material in the filter
    • B01D33/48Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
    • B01D33/50Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/06Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
    • B01D33/11Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for outward flow filtration

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  • 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)

1. Zastrzezenie patentowe Urzadzenie do ciaglego odwadniania w procesie hydromechanicznej i mechanicznej obróbki sflokulowa¬ nych mulów, posiadajace obracajacy sie cylinder, zaopatrzony wewnatrz w elementy aglomerujace, korzystnie w progi przewalowe i/lub slimak transportujacy, znamienne tym, ze powierzchnie cylindra 3 stanowi sito o zmiennej w sposób ciagly wzdluz pobocznicy, wielkosci oczek, do którego górnej czesci przylegaja dysze 8 nadmuchu sprezonego powietrza. Prac. Poligraf. UP PRL naklad 120+18 Cena 45 zl"1. Claim A device for continuous dewatering in the process of hydromechanical and mechanical treatment of flocculated silts, having a rotating cylinder, provided inside with agglomerating elements, preferably with a shaft shoulder and / or a conveyor screw, characterized in that the cylinder surface 3 is a screen with variable continuously along the sidewall, mesh size, the upper part of which is adjoined by the compressed air nozzles 8. Wash. Typographer. UP PRL, edition 120 + 18 Price: PLN 45 "
PL1976188312A 1976-03-27 1976-03-27 MACHINE FOR CONTINUOUS DEWATERING IN THE PROCESS OF HYDROMECHANICAL AND MECHANICAL PROCESSING OF FLOCKED MULLS PL104587B1 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

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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