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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
    Wyświetlanie 1-2 z 2

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