Coalescence Filtration with an Unwoven Fabric Barrier in Oil Bilge Water Separation on Board Ships

2017 ◽  
pp. 115-122
Keyword(s):  
Water Separation ◽  
Bilge Water

scholarly journals Oil–Water Separation Techniques for Bilge Water Treatment

2020 ◽  
Author(s):  
Nurul Aini Amran ◽  
Siti Nor Adibah Mustapha
Keyword(s):  
Water Treatment ◽  
Biological Processes ◽  
Water Separation ◽  
Separation Techniques ◽  
International Convention ◽  
Advantages And Disadvantages ◽  
Bilge Water ◽  
Coagulation And Flocculation ◽  
Oil Water Separation ◽  
Oil Water

Discharging accumulated bilge water from the ship is very important in order to maintain its stability and safety. However, the bilge water that contains contaminants, including waste oils and oily wastes, must be treated prior discharging to the sea. The International Convention for the Prevention of Pollution from Ships (MARPOL) has set strict oil discharge limit in order to minimize sea pollution. Thus, an efficient oil–water separator must be installed to separate the oil from the bilge water. This chapter introduces and discusses the working mechanisms, as well as advantages and disadvantages of the available oil–water separation techniques for bilge water treatment, which include gravitational, centrifugation, flotation, coagulation and flocculation, biological processes as well as absorption and adsorption.

Effect of Process Factors on Pervaporation Dehydration of Isopropanol

2017 ◽  
Vol 68 (6) ◽  
pp. 1302-1305
Author(s):  
Ali A. A. Al Janabi ◽  
Oana Cristina Parvulescu ◽  
Bogdan Trica ◽  
Tanase Dobre
Keyword(s):  
Ceramic Membrane ◽  
Membrane Surface ◽  
Water System ◽  
Surface Model ◽  
Feed Water ◽  
Mixture Flow ◽  
Water Separation ◽  
Membrane Area ◽  
Operation Temperature ◽  
Process Factors

The paper aimed at studying the performances of pervaporation separation of isopropanol-water system using a Pervatech ceramic membrane at various values of feed mixture flow rate (F=1000 kg/hr), feed water mass fraction (xF=0.1-0.2), operation temperature (t=60-90 �C), permeate pressure (pP=1000-9000 Pa) and water separation degree (sW=0.9, 0.95). Membrane total flux and separation factor were predicted applying a second order response surface model with 3 factors, i.e., xF, t and pP. An algorithm for estimating the membrane surface area was presented. Membrane area increased with sW and xF and its lowest values (A=13 m2 for xF=0.1 and A=24 m2 for xF=0.2) were attained for t=60 �C and pP=9000 Pa. These findings could be applied for optimizing the process of isopropanol dehydration by pervaporation.

Complex membrane of cellulose and chitin nanocrystals with cationic guar gum for oil/water separation

2019 ◽  
Vol 136 (37) ◽  
pp. 47947 ◽  
Author(s):  
Hajo Yagoub ◽  
Liping Zhu ◽  
Mahmoud H. M. A. Shibraen ◽  
Xiaowei Xu ◽  
Dafaalla M. D. Babiker ◽  
...  
Keyword(s):  
Guar Gum ◽  
Water Separation ◽  
Complex Membrane ◽  
Oil Water Separation ◽  
Oil Water

Durable superhydrophilic coatings formed for anti-biofouling and oil–water separation

2016 ◽  
Vol 506 ◽  
pp. 22-30 ◽  
Author(s):  
Xiangde Lin ◽  
Miso Yang ◽  
Hyejoong Jeong ◽  
Minwook Chang ◽  
Jinkee Hong
Keyword(s):  
Water Separation ◽  
Oil Water Separation ◽  
Oil Water
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