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    Tytuł:
    Własności filtracyjne zawiesiny po wirówkach DECANTER po dodaniu flokulantu Magnafloc 919
    Filtering properties of suspension from the DECANTER centrifuge with Magnafloc 919 flocculant addition
    Autorzy:
    Palica, M.
    Gierczycki, A.
    Lemanowicz, M.
    Powiązania:
    https://bibliotekanauki.pl/articles/1819799.pdf
    Data publikacji:
    2009
    Wydawca:
    Politechnika Koszalińska. Wydawnictwo Uczelniane
    Tematy:
    zawiesina
    filtracja
    wirówka
    flokulent
    DECANTER
    suspension
    flocculant
    Opis:
    The results of an experimental research on dewatering of dump suspensionfrom the DECANTER centrifuge are presented in this paper. The suspension was taken from one of mines of the Jastrzębska Spółka Węglowa. This research allowed one to determine so called filtration parameters needed for the modeling of pressure filtration with cake compression. Some physical properties (density, mass fractions, moisture content, porosity, resistance of filter medium) as well as the kinetic constant coefficients (K and K') were concerned. The data was collected for the original suspension, i.e. liquid from the DECANTER centrifuge, and for the suspension with an addition of Magnafloc 919, flocculant used for flotoconcentrate, in the amount range between 10÷80 g/1 Mg of dry product, while the used dosage is 30 g/1 Mg. It was found that the addition of flocculant caused the increase of cake porosity and cake compressibility coefficient calculated according to the Tiller and Leu equation. Simultaneously, in small extends, the addition of flocculant resulted in increased cake's moisture content after the pressure filtration which is an unfavorable effect. On the other hand, it increased the constant kinetic coefficients K and K' in comparable conditions, enlarged mean arithmetic diameter of grains and accelerated the sedimentation process. The dosage of 30 g/1 Mg used by the maintenance personnel appears to be correct as well as the used filter cloth PT 912. One of the most interesting conclusion from this work is that the cake moisture content was lower after the pressure filtration than after the centrifuge filtration - this observation applies to the original dump suspension as well as to the one with the addition of flocculant. It is worth to emphasize that in case of the flocculant addition between 10÷30 g/1 Mg, Magnafloc 919 significantly influenced filtration properties of dump suspension. In case of the addition above 30 g/1 Mg that influence became very weak, therefore the application of the excessive addition is pointless from thetechnical point of view. The comparison of filtration parameters for dump suspension without and with the addition of flocculant suggests that there should not be any operating difficulties with the filtration process after a change of dewatering technology based on the usage of a settling tank for the dump suspension, recirculation of clear liquid and mixing of sludge with flotoconcentrate. One of advantages of this solution is the water - sludge circulation closure but it is connected with a greater DECANTER centrifuge load or with the addition of a supplementary centrifuge to the system.
    Źródło:
    Rocznik Ochrona Środowiska; 2009, Tom 11; 823-836
    1506-218X
    Pojawia się w:
    Rocznik Ochrona Środowiska
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Wpływ dodatku flokulantu Magnafloc 919 na przebieg filtracji wirowej podekantacyjnej zawiesiny odpadowej
    Influence of Magnafloc 919 flocculant dosage on centrifugal filtration of post-decantation dump suspension
    Autorzy:
    Palica, M.
    Dolina, A.
    Gierczycki, A.
    Kolorz, S.
    Powiązania:
    https://bibliotekanauki.pl/articles/1819801.pdf
    Data publikacji:
    2009
    Wydawca:
    Politechnika Koszalińska. Wydawnictwo Uczelniane
    Tematy:
    flokulant
    filtracja wirowa
    Magnafloc 919
    zawiesina odpadowa
    dump suspension
    flocculant
    Opis:
    Niniejszy artykuł jest kontynuacją cyklu prac Palicy i współpracowników dotyczących separacji fazowej zawiesin zrzutowych po wirówkach DECANTER, na których odwadnia się flotokoncentraty węgli kamiennych [1÷12]. Wiele prac w tej problematyce począwszy od lat 70-tych prowadził Piecuch i współpracownicy.
    In the paper experimental results dealing with centrifugal filtration of postdecantation dump suspension after the DECANTER centrifuge and obtained in a coal mine of "Jastrzębska Spółka Węglowa". Magnaflog-919 flocculant, used by operating service, was added to suspension. The suspension is characterized by very fine grainsize increasing during subsequent cycles, what leads, in consequence, to its replacement. This is connected not only with water and deposition costs but also with the losses of solid phase which is about 81% coal. In the mentioned coal mine 30 g of dry Magnaflog-919 flocculant per 1 Mg of dry product is added to flotoconcentrate. Floccu lant is dosed in a form of 0.1% gel. Therefore it appears a question if during dewatering of dump suspension containing 7÷8% of solid phase (using e.g. centrifugal or pressure filtration) flocculant should be again added, and if an answer is positive - in what amount? As a measure of dewatering efficiency, the final moisture content in cake obtained during centrifugal filtration for defined parameters of the laboratory centrifuge (adapted to a filtration centrifuge) was assumed. The test were carried out in the range of multiplication coefficient ? = a/g = 251.3÷1786.8 and centrifugal time ? = 280÷1800 s for dump suspension containing a base flocculant dose of 30 g/1 Mg, and doses of 15 and 60 g/1 Mg. Each experimental run consists of 6 values of ? and 7 of ? (altogether 42x4 points). For each experimental run tri-parameter correlations in a form of w = f(a/g, ?) = exp[A(a/g)b ?c] + D with regression coefficient R2>0.983 were elaborated. It should be noted that however the correlations quite well describe the process they have no theoretical bases. It was stated that the Magnaflog-919 flocculant dosage in the range 15÷60 g/1 Mg of dry product, for the same a/g and ?, produced an increase of moisture content in cake after centrifugation in comparison with values obtained for dump suspension. This, rather unexpected effect, can be explained by disruption of large flocs during decantation in DECANTER centrifuges and deposition of filtrate in smaller fragments or newly created flocs, for which centrifugal forces were not sufficiently high to remove it from cake. It was proved by higher values of moisture content in cake after centrifugal filtration in comparison with pressure filtration with cake compression. It was also stated the a good usability of filter cloth PT 912 for filtration, while an additive of flocculant accelerated sedimentation. Taking these into account, it seems that dewatering of dump suspension should be carried on in two stages. In the first stage suspension (with 30 g of flocculant per 1 Mg) should be directed to a settling tank, clarified liquid from this apparatus should be used in recirculation. In the second stage post-sedimentation slurry should be directed to a mixing process unit with flotoconcentrate, situated before DECANTER centrifuges.
    Źródło:
    Rocznik Ochrona Środowiska; 2009, Tom 11; 1063-1075
    1506-218X
    Pojawia się w:
    Rocznik Ochrona Środowiska
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
    Tytuł:
    Zmiana właściwości filtracyjnych flotokoncentratu węglowego poddanego filtracji wirowej po sonifikacji flokulantu
    Change of filtration properties of coal flotoconcentrate subjected to the centrifugal filtration after flocculant sonication
    Autorzy:
    Palica, M.
    Drzazga, M.
    Gierczycki, A.
    Gozdek, A.
    Thullie, J.
    Powiązania:
    https://bibliotekanauki.pl/articles/1819349.pdf
    Data publikacji:
    2012
    Wydawca:
    Politechnika Koszalińska. Wydawnictwo Uczelniane
    Tematy:
    flotokoncentrat węgla kamiennego
    filtracja
    sonifikacja
    osad
    Opis:
    Vacuum filtration is widely used in dehydration of the coal flotoconcentrate. Inspite of the application of flocculants, it gives post-filtration suspension humidity of ca. 27-28%. Suspension humidity may be significantly decreased as a result of the centrifugal filtration. Investigated flotoconcentrate suspension contained ca. 31% of solids and its density was ca. 1087 [kg/m3]. Flocculant Magnafloc 336 was added to the suspension in a proportion 70 g/l Mg of dry product. During the simultaneously performed investigation on vacuum filtration ([4]) it was shown that applied dosage is too small. Therefore, an additional flocculant portion of 40 g/l Mg of dry product is advisable. It enables one to obtain a product of less humidity. It was also stated that, in comparison to a nonsonicated flocculant, a treatment of the additional dosage by an ultrasound field of 20 [kHz] for 6 [s] results in an additional effect of dehydration. Investigations of the centrifugal filtration were carried out for the following parameters of a laboratory centrifuge: tau = 5-30 min, a/g = 251.3-1969.9. Investigation series for given suspension (without additional flocculant, addition of 40 g/l Mg and sonicated addition of 40 g/l Mg) included 7 centrifugation times and 6 values of the multiplication coefficient. It means 42 measurement points. All examinations were carried out for the same filtration cloth PT-912. Empirical triparametric correlations w(pl) = f (a/g,tau) were developed. The value of R-2 of the correlation is not lower than 0.9443 for investigated suspensions. Moreover, particle size distribution as well as sedimentation tests of examined suspensions were performed. It was stated that although addition of the extra flocculant dosage causes the decrease of humidity of the filtration cake significantly as a result of centrigugal filtration, the sonication of the flocculant was beneficial for final dehydration, however the changes were less noticable. For the most important working parameters of the centrifuge, i.e. a/g = 1970 and tau = 1800 s, for sonicated flocculant Magnafloc addition w(pl) approximate to 16.5% was obtained. Physical explanation of the flocculant sonication effect is a formation of smaller but more stable aggregates and the considerably lower amount of micrograins in comparison to a technological suspension. This suggestion is confirmed not only by sedimentation tests and grain analyses, but also by other coal flotoconcentrate investigations published in [7, 10], considering an influence of the flocculate sonication on w(pl) during the pressure filtration.
    Źródło:
    Rocznik Ochrona Środowiska; 2012, Tom 14; 752-760
    1506-218X
    Pojawia się w:
    Rocznik Ochrona Środowiska
    Dostawca treści:
    Biblioteka Nauki
    Artykuł
      Wyświetlanie 1-3 z 3

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