ULEKSİTİN SO2 İLE DOYURULMUŞ SULARDA ÇÖZÜNMESİNDEN ELDE EDİLEN SÜSPANSİYONLARIN ÇAPRAZ-AKIŞ MİKROFİLİTRASYONU

Bu çalışmada uleksitin SO2 ile doyurulmuş sularda 92oC de çözündürülmesi sonucu elde edilen CaSO3 ve MgSO3 süspansiyonlarının mikrofiltrasyonu boyunca, transmembran basıncı, çapraz akış hızı ve membran por boyutlarının süzme özellikleri üzerindeki etkileri belirlenmiştir. Sızıntı akışı, 150-400 kPa transmembran basıncında, 3,8-8,3 L.dakika-1 çapraz akış hızında ve çeşitli por boyutlarına sahip membranlar kullanılarak ölçülmüştür. Partikül konsantrasyonu 22,9 g.L-1, sıcaklık 30oC ve pH 7,33’te sabit tutulmuştur. Akıların ve spesifik kek dirençlerinin tansmembran basıncının ve çapraz akış hızının artması ile arttığı tespit edilmiştir. Keza, akı, membran por boyutlarından çok fazla etkilenmemiş, spesifik kek dirençleri de düzenli bir dağılım göstermemiştir. İlaveten kekin sıkıştırılabilir bir kek olduğu bulunmuştur

CROSS-FLOW MICROFILTRATION OF SUSPENSIONS OBTAINED BY DISSOLVING ULEXITE IN SO2 SATURATED WATER

In this study, the effect of the transmembrane pressure, cross-flow rate and membrane pore sizes on the filtration properties have been investigated during the microfiltration of suspensions containing CaSO3 and MgSO3 from dissolving of ulexite in SO-saturated water at 92oC. Permeate has been measured at 3.8-8.3 LPM cross-flow rate and 150-400 kPa transmembrane pressure by using membranes with various pore size. Particle concentration has been kept constant at 22.9 g.mL-1, temperature at 30oC and pH at 7.33. As result, it has been determined that specific cake resistance increases by increasing transmembrane pressure and cross-flow rate, and also, permeate rate increases with increasing transmembrane pressure and cross-flow rate. In has been seen that specific cake resistances and permeate rates do not change with membrane type and pore size. In addition it has been found the cake can be compact

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