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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
Tytuł:
Periodyczna filtracja wirowa zawiesiny zrzutowej po wirówkach BIRDa, zawierającej dodatek flokulantu Magnaflog
Batch centrifugal filtration of dump suspension containing Magnaflog 336 flocculant obtained in the BIRD centrifuge
Autorzy:
Palica, M.
Pęczek, K.
Kurowski, Ł.
Niemirowski, J.
Powiązania:
https://bibliotekanauki.pl/articles/1825950.pdf
Data publikacji:
2008
Wydawca:
Politechnika Koszalińska. Wydawnictwo Uczelniane
Tematy:
filtracja
flokulant
Magnaflog 336
filtracja wirowa
wirówki filtracyjne
Opis:
A course of centrifugal filtration of dump suspension with and without Magnaflog 336 flocculant of concentration 1 g/m3 susp. was compared in the paper. In both cases the filter cloth PT 912 selected in batch filtration tests was used. Similarly, a flocculant dosage was chosen in additional tests in which an influence of the flocculant amount on pressure filtration was checked. It was proved that practically justifiable dosage should be slightly smaller than abovementioned (1.7 g/m3 susp.). On basis of 42 tests for suspension without flocculant and 42 tests for suspension containing flocculant, two dependencies describing dewatering intensity (final moisture content in cake) as a function of the acceleration simplex and centrifugation time were found. They are as follows w exp [A (a g)B C ] D pl = ? + where constants and exponents are given in Tab.2. The dependencies are valid with good accuracy. For most common values of (a/g) and ? used in experiments, and suspension with and without flocculant, the final moisture content of cake was in the range wpl = 37.2 - 37.6 %. Also, what was very important, filtrate was quite clear and could be turned backward to a process line. Additional experiments, such as PSD analysis and sedimentation tests, proved that the deposition of suspension and addition of flocculant favour agglomeration thus facilitating (accelerating) phase separation. Selected data of PSD analyses performed in the particle size analyser Analysette 22 of Fritsch are gathered in Tab.3. The sedimentation tests proved a decrease of the turbidity zone after 2 hours to such extent that it is possible to reduce the amount of suspension at least 5 times. Roughly calculations indicated that solid phase fraction in post-sedimentation sludge increased from about uz = 0.045 to uz = 0.173. Therefore, such sludge can be easier separated, and moreover (very important), its amount is many times smaller than the amount of inlet suspension. This implies that the initial separation of inlet suspension is strongly advisable. On the other hand, no significant differences between sedimentation with and without addition of Magnaflog 336 flocculant were observed. It seems that the turn-back of clarified liquid to circulation and a supply of sludge from a settling tank to inlet suspension, or alternatively the filtration of sludge after a settling tank should be the relatively cheaper and advisable method of dewatering
Źródło:
Rocznik Ochrona Środowiska; 2008, Tom 10; 275-288
1506-218X
Pojawia się w:
Rocznik Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
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