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008 160804t2016 my da f abm 000 0 eng d
020 _aTHE0001015(Local)
039 9 _a201905241619
_bnazirah
_c201710171158
_daishah
_c201612081021
_dsaini
_y201608041538
_zsaini
040 _aUMP
090 _aFKKSA .S56 2016 r Thesis
100 1 _aShnain, Zainab Yousif
245 1 0 _aSolid-polymer-surfactant complexes for enhancing the flow in pipelines /
_cZainab Yousif Shnain
260 _aKuantan, Pahang :
_bUMP,
_c2016
300 _axxi, 270 p. :
_bill. (some col.) ;
_c30 cm. +
_e2 CD-ROM
500 _aFaculty of Chemical & Natural Resources Engineering
502 _aThesis (Doctor of Philosophy in Chemical Engineering) -- Universiti Malaysia Pahang – 2016
504 _aBibliography : p. 215-230
520 3 _aEddies which arise as a result of the turbulent nature of fluids pumped through pipelines is a major challenge which contributes to drag. Such not only increases the time of liquid transportation, but contributes to massive energy dissipation. As a result, efforts are being made to contain these anomalies but a consensus has not been reached. Thus, the initiation of this current research. This work introduces an economically feasible technique for enhancing the drag reduction and mechanical degradation of known polymeric additives through the formation of certain complexes with polar surface active agents (surfactants). Such was achieved by using two polymeric additives: Polyacrylamide and Sodium Carboxyl Methyl Cellulose, two surfactants: Sodium Dodecyl-Benzene Sulfonate (SDS) and Triton X-45 and Nano particles of Fumed silica to form complexes. Three phases were involved in the experiment-the use of Rotating Disk Apparatus (RDA) to examine drag reduction, mechanical resistance and stability of the additives, the Transmission Electron Microscopy (TEM) to examine the morphology of the complexes, the drag reduction and shear stability of the investigated solutions using a closed loop pipeline system. Overall, the results obtained from all the stages of the experiment showed that drag reduction increased as the concentration increased. The highest drag reduction for polymer was 48% at 2000ppm while the complex of Polyacrylamide and Sodium dodecyl-benzene sulfonate gave 54% which made complexes better. This showed optimum performance against their 33% and 35% respective individual DR. Adding fume silica to this mixture inhibits their degradation and yielded %DR of (47, 48, 51, 54, 58), (45, 48, 54, 55, 57) and (56, 57, 61, 63, 68) for polymer-surfactant-fumed-silica powder at (500, 1000, 1500, 1700, 2000)PPM concentration respectively.However, the pipe results obtained for 2000ppm was 7826.618. Results for (PAM-Triton X-45-fumed silica) complex was 85.8 % drag reduction and for fumed silica-Triton X-45 complex (fumed silica-PAM), it was 79.2% and 76.7% respectively. Other results such as fumed silica alone, surfactant solution and polymer at 2000ppm showed 63.2 %, 62.6% and 59.5% drag reduction respectively. Overall, about 85.8% DR was achieved in the study, which is the power saving possible in transporting the fluid through pipelines. A mathematical expression was developed to delineate the real mechanism of DR. As a conclusion, new, greener DRAs were successfully introduced and their effectiveness in improving the flow was proven experimentally. According to the TEM images, it is confirmed that complexes are effectively formed in the present work and new aggregated structure can contribute significantly to the drag reduction and polymer shear resistance enhancement.
610 2 0 _aFaculty of Chemical & Natural Resources Engineering
_xDissertations
650 0 _aUniversities and Colleges
_xDissertations
650 0 _aTheses
856 4 0 _uhttp://ecollib.ump.edu.my/3502/
_zLibrary access only
999 _aVIRTUA40
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