Investigation the foam dynamics capacity of SDS in foam generator by affecting the presence of organic and inorganic contaminant

Author(s):  
Bode Haryanto ◽  
M. Z. Siswarni ◽  
Yosef C. H. Sianipar ◽  
Tongam M. A. Sinaga ◽  
Imam Bestari
Author(s):  
Yingchun Liu ◽  
Mingju Jing ◽  
Rongcen Xu ◽  
Xiaoyang Luan ◽  
Juncheng Jiang ◽  
...  

2012 ◽  
Vol 108 (19) ◽  
Author(s):  
M. Stoffel ◽  
S. Wahl ◽  
E. Lorenceau ◽  
R. Höhler ◽  
B. Mercier ◽  
...  

2016 ◽  
Vol 39 ◽  
pp. 173-180 ◽  
Author(s):  
Brian Harding ◽  
Bin Zhang ◽  
Yi Liu ◽  
Hao Chen ◽  
M. Sam Mannan

2007 ◽  
Vol 1 (10) ◽  
pp. 425-429 ◽  
Author(s):  
J. F. Fry ◽  
R. J. French

2014 ◽  
Vol 679 ◽  
pp. 20-24 ◽  
Author(s):  
Mohd Mustafa Al Bakri Abdullah ◽  
Zarina Yahya ◽  
Muhammad Faheem Mohd Tahir ◽  
Kamarudin Hussin ◽  
Mohammed Binhussain ◽  
...  

This paper presents the mechanical properties of a lightweight geopolymer concrete synthesized by the alkali-activation of a fly ash source (FA) produced by mixing a paste of geopolymer with foam produced by using NCT Foam Generator. Two curing conditions are used, curing at room temperature and curing in an oven with a constant temperature which is 60 oC. Bulk density showed that fly ash-based geopolymer lightweight concrete is light with the density of 1225 kg/m3 - 1667 kg/m3 with an acceptable compressive strength of 17.60 MPa for the density of 1667 kg/m3.


2003 ◽  
Vol 2 (1) ◽  
Author(s):  
J. Gylys ◽  
M. Jakubcionis ◽  
S. Sinkunas ◽  
T. Zdankus

The model of heat exchanger was investigated experimentally. This model consists of three vertical lines of horizontal tubes with five tubes in each. Tubes were arranged in a staggered order. Heat transfer of staggered bundle of tubes to downward static stable foam flow was investigated experimentally. Heat transfer dependence on specific gas and liquid velocity was determined. Dependence of volumetric void fraction of foam on heat transfer was investigated also. Heat transfer rate dependence on tube position in the line of tube bundle was investigated experimentally. It was established that heat transfer rate highly depends on tube position in the line. Influence of tube position on heat transfer from tube bundle in upward foam flow was compared. Heat transfer dependence on tube position in the bundle was investigated experimentally also. Influence of wall of foam generator on heat transfer to sideline of tubes was established. Experimental results of heat transfer of bundle of tubes to downward static stable foam flow were generalized using dependence between Nusselt and Reynolds numbers.


Author(s):  
Jonas Gylys ◽  
Stasys Sinkunas ◽  
Tadas Zdankus ◽  
Vidmantas Giedraitis

Gas-liquid foam due to especially large inter-phase contact surface can be used as a coolant. An experimental investigation of the staggered and in-line tube bundles’ heat transfer to the vertically upward and downward laminar foam flow was performed. The experimental setup consisted of the foam generator, vertical experimental channel, tube bundles, measurement instrumentation and auxiliary equipment. It was determined dependency of heat transfer intensity on flow parameters: flow velocity, direction of flow, volumetric void fraction of foam and liquid drainage from foam. Apart of this, influence of tube position in the bundle to heat transfer was investigated. Foam flow structure, distribution of the foam’s local void fraction and flow velocity in cross-section of the channel were the main factors which influenced on heat transfer intensity of the different tubes. Experimental investigation showed that the heat transfer intensity of the frontal and further tubes of the bundles to vertical foam flow is different in comparison with one-phase fluid flow. The results of the experimental investigation are presented in this paper.


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