Preview

Role of Risk Management in Managing Price Volatility in the Global Oil and Gas Market

Best Essays
Open Document
Open Document
5131 Words
Grammar
Grammar
Plagiarism
Plagiarism
Writing
Writing
Score
Score
Role of Risk Management in Managing Price Volatility in the Global Oil and Gas Market
-------------------------------------------------
Abstract
In the last few decades, membrane technology has been a great attention for gas separation technology especially for natural gas sweetening. The intrinsic character of membranes makes them fit for process escalation, and this versatility could be the significant factor to induce membrane technology in most gas separation areas. Membranes were synthesized with various materials which depended on the applications. The fabrication of polymeric membrane was one of the fastest growing fields of membrane technology. However, polymeric membranes could not meet the separation performances required especially in high operating pressure due to deficiencies problem. The chemistry and structure of support materials like inorganic membranes were also one of the focus areas when inorganic membranes showed some positive results towards gas separation. However, the materials are somewhat lacking to meet the separation performance requirement. Mixed matrix membrane (MMM) which is comprising polymeric and inorganic membranes presents an interesting approach for enhancing the separation performance. Nevertheless, MMM is yet to be commercialized as the material combinations are still in the research stage. This paper highlights the potential promising areas of research in gas separation by taking into account the material selections and the addition of a third component for conventional MMM.
-------------------------------------------------
1. Introduction
Natural gas can be considered as the largest fuel source required after the oil and coal [1]. Nowadays, the consumption of natural gas is not only limited to the industry, but natural gas is also extensively consumed by the power generation and transportation sector [2]. These phenomena supported the idea of going towards sustainability and green technology as the natural gas is claimed to generate less-toxic gases like carbon dioxide (CO2) and nitrogen oxides () upon



References: 1. Soregraph, Key World Energy Statistic, The International Energy Agency, 2010. 2. Longterm Outlook to 2030, Natural Gas Demand and Supply, The European Union of The Natural Gas Industry, 2010. 4. A. Wan and A. Rusmidah, Natural Gas, Universiti Teknologi Malaysia, 2010. 5. D. David and D. Kishore, Recent Development in CO2 Removal Membrane Technology, UOP, 1999. 6. M. I. Fauzi and A. Akkil, Meeting Technical Challenge in Developing High CO2 Gas Field Offshore, Petronas Carigali Sdn. Bhd., 2008. 7. Fuels Providers, Natural Gas Specs Sheet, The National Petroleum Agency, 2002. 8. Separation Process, Membrane Separation Process, Membrane Properties, 1998. 9. Separation Process, Introduction to Membrane, Chapter 1, 1998. 10. K. Scott, Membrane Separation Technology, Scientific & Technical Information, Oxford, UK, 1990. 11. H. Strathmann, “Membrane separation processes: current relevance and future opportunities,”AIChE Journal, vol. 47, no. 5, pp. 1077–1087, 2001. View at Publisher · View at Google Scholar ·View at Scopus 12 13. A. F. Ismail and L. I. B. David, “A review on the latest development of carbon membranes for gas separation,” Journal of Membrane Science, vol. 193, no. 1, pp. 1–18, 2001. View at Publisher ·View at Google Scholar · View at Scopus 14 15. J. A. Ritter and A. D. Ebner, “Carbon dioxide separation technology—R&D needs for the chemical and petrochemical industries,” Chemical Industry Vision 2020, 2007. 16. T. Visser and M. Wessling, “When do sorption-induced relaxations in glassy polymers set in?”Macromolecules, vol. 40, no. 14, pp. 4992–5000, 2007. View at Publisher · View at Google Scholar· View at Scopus 17 18. J. D. Wind, D. R. Paul, and W. J. Koros, “Natural gas permeation in polyimide membranes,”Journal of Membrane Science, vol. 228, no. 2, pp. 227–236, 2004. View at Publisher · View at Google Scholar · View at Scopus 19 20. A. J. Bird and D. L. Trimm, “Carbon molecular sieves used in gas separation membranes,”Carbon, vol. 21, no. 3, pp. 177–180, 1983. View at Scopus 21 24. L. A. Pessan and W. J. Koros, “Isomer effects on transport properties of polyesters based on bisphenol-A,” Journal of Polymer Science B, vol. 31, no. 9, pp. 1245–1252, 1993. View at Publisher· View at Google Scholar · View at Scopus 25 26. X. Gao, Z. Tan, and F. Lu, “Gas permeation properties of some polypyrrolones,” Journal of Membrane Science, vol. 88, no. 1, pp. 37–45, 1994. View at Publisher · View at Google Scholar ·View at Scopus 27 32. C. Y. Tsai, S. Y. Tam, Y. Lu, and C. J. Brinker, “Dual-layer asymmetric microporous silica membranes,” Journal of Membrane Science, vol. 169, no. 2, pp. 255–268, 2000. View at Publisher ·View at Google Scholar · View at Scopus 33 34. D. E. W. Vaughan, “The synthesis and manufacture of zeolites,” Chemical Engineering Progress, vol. 84, no. 2, pp. 25–31, 1988. 35. M. A. Carreon, Novel Membranes for Efficient CO2 Separation, University of Lousville, 2011. 36. S. Kulprathipanja, R. W. Neuzil, and N. N. Li, “Separation of fluids by means of mixed matrix membranes in gas permeation,” US Patent 4,740,219, 1988. 37. T. M. Gür, “Permselectivity of zeolite filled polysulfone gas separation membranes,” Journal of Membrane Science, vol. 93, no. 3, pp. 283–289, 1994. View at Publisher · View at Google Scholar ·View at Scopus 38 39. C. M. Zimmerman, A. Singh, and W. J. Koros, “Tailoring mixed matrix composite membranes for gas separations,” Journal of Membrane Science, vol. 137, no. 1-2, pp. 145–154, 1997. View at Publisher · View at Google Scholar · View at Scopus 40 43. M. G. Süer, N. Baç, and L. Yilmaz, “Gas permeation characteristics of polymer-zeolite mixed matrix membranes,” Journal of Membrane Science, vol. 91, no. 1-2, pp. 77–86, 1994. View at Publisher · View at Google Scholar · View at Scopus 44 46. S. Kulprathipanja, “Review of recent progress in mixed matrix membranes,” Membrane Technology, vol. 105, pp. 6–8, 2000. 47. R. Mahajan and W. J. Koros, “Factors controlling successful formation of mixed-matrix gas separation materials,” Industrial and Engineering Chemistry Research, vol. 39, no. 8, pp. 2692–2696, 2000. View at Scopus 48 55. D. Sen, Polycarbonate based zeolite 4A filled mixed matrix membranes: preparation, characterization and gas separation performances [Ph.D. thesis], Middle East Technical University, 2008. 56. D. R. Paul and D. R. Kemp, “Diffusion time lag in polymer membranes containing adsorptive fillers,” Journal of Polymer Science C, no. 41, pp. 79–93, 1973. View at Scopus 57 66. H. Ohno, M. Yoshizawa, and W. Ogihara, “Development of new class of ion conductive polymers based on ionic liquids,” Electrochimica Acta, vol. 50, no. 2-3, pp. 255–261, 2004. View at Publisher · View at Google Scholar · View at Scopus 67 74. C. A. Oral, R. D. Noble, and S. B. Tantekin-Ersolmaz, “Ternary mixed-matrix membranes containing room temperature ionic liquids,” in Proceedings of the North American Membrane Society Conference (NAMS '11), 2011.

You May Also Find These Documents Helpful

  • Good Essays

    Carbon dioxide and oxygen both easily cross a membrane because they are both nonpolar, small molecules.…

    • 855 Words
    • 4 Pages
    Good Essays
  • Powerful Essays

    Actual membranes adhere more strongly to water than do artificial membranes composed only of phospholipids.…

    • 3885 Words
    • 16 Pages
    Powerful Essays
  • Satisfactory Essays

    For NaCl, which MWCO membrane(s) provided for the net movement of water without movement of NaCl?…

    • 432 Words
    • 2 Pages
    Satisfactory Essays
  • Powerful Essays

    The experiment performed was Experiment IV: Fluid Flow Meters and Tray Hydraullics. The group was composed of Alex Long, Khanh Ho, Tricia Heitmann and myself. The first day of experimentation was April 16, 2013. On this day, Alex and I ran the sieve tray apparatus to study the vapor and liquid tray hydraulics parameters for sieve type crossflow distillation trays. Tricia and Khanh ran the fluid flow apparatus to determine the operating characteristics of the Venturi and orifice meters.…

    • 6399 Words
    • 26 Pages
    Powerful Essays
  • Satisfactory Essays

    Exam 2 Study Guide

    • 983 Words
    • 4 Pages

    2. What factors affect membrane fluidity, and how? Why is the cell membrane referred to as a “fluid matrix”?…

    • 983 Words
    • 4 Pages
    Satisfactory Essays
  • Good Essays

    June 13 Membranes

    • 887 Words
    • 3 Pages

    THE MEMBRANES OF DIFFERENT TYPES OF CELLS ARE INVOLVED IN MANY DIFFERENT FUNCTIONS – 25 MARKS…

    • 887 Words
    • 3 Pages
    Good Essays
  • Good Essays

    dfdf

    • 845 Words
    • 4 Pages

    Liquid carbon disulfide reacts with elemental oxygen to yield carbon dioxide gas and sulfur dioxide gas.…

    • 845 Words
    • 4 Pages
    Good Essays
  • Better Essays

    This experiment gave a visual understanding of osmosis and diffusion. The first experiment proved that solutes would move down a concentration gradient if permeable to the selective membrane. The second experiment proved different solute concentrations affect the movement of water, depending on the solute concentration inside the cell. The purpose of this lab was to look for different solutes that can cross an artificial membrane and to observe the effect of different concentrations of sucrose on the mass of a potato cell. Results for Part One suggested that the molecular weight of albumin and starch was too large to pass through the dialysis tube, but glucose and sodium sulfate molecules were small enough to pass through the dialysis tube. Also, a decrease in water weight occurred due the dialysis tube being placed in a hypertonic solution. Results for Par Two showed the potato cell having a molar concentration of 0.2734, which caused sucrose concentrations above 0.2 M to have a decrease in mass. Inversely, sucrose concentrations below 0.2 M caused an increase in mass.…

    • 2179 Words
    • 9 Pages
    Better Essays
  • Powerful Essays

    To keep it as simple as possible, (K.I.S.S.) this topic involves the study of: 1. POLYMERS FROM PETROCHEMICALS & BIOMASS…

    • 15670 Words
    • 63 Pages
    Powerful Essays
  • Powerful Essays

    The reaction would be cellulose with acetic anhydride in the presence of a catalyst, such as sulfuric acid. This would result in the formation of acetylated cellulose, the main component of the membrane, and acetic acid, a byproduct. The cellulose based membranes were easy to make and are more resistant to chlorine than other reverse osmosis membranes. But they are sensitive to changes in pH and temperature, and they also tend to break down in the presence of water over time. Then came along the thin film composite membranes, first synthesized by John Cadotte. This membrane was composed of a polyamide coating made through the reaction between m-phenylenediamine and trimesoyl chloride. This new membrane allowed for higher salt rejection and water flow, while allowing for a reduced pressure to be applied to counteract the osmotic pressure. But when the polyamide comes into contact with chlorine, it disrupts the hydrogen bonding breaking down the polymer and greatly reducing salt…

    • 1888 Words
    • 8 Pages
    Powerful Essays
  • Powerful Essays

    Pettruci, R.H., Harwood, W.S., Herring, F.G.. (2004) General Chemistry: Principles and Modern Applications 8th Edition. Pearson Education South Asia Pte. Ltd. Singapore…

    • 2594 Words
    • 11 Pages
    Powerful Essays
  • Good Essays

    The purpose of this session is to demonstrate the concept of a single phase gas flow through a porous media. The method that used in this lab is the nitrogen gas (Reslab digital gas permeameter). In addition, the gas flow expressed by the Darcy’s equation which relates volumetric flow and pressure drop with the properties of the fluid and media.…

    • 1944 Words
    • 8 Pages
    Good Essays
  • Powerful Essays

    synthesis organic polymers

    • 3697 Words
    • 16 Pages

    Organic polymers are macromolecules that are composed of smaller molecules called monomers. There are two main groups of polymers: natural polymers and unnatural (synthetic) polymers. Natural polymers include proteins such as cellulose and starch and are a necessity for our existence. On the other hand, synthetic polymers such as the polycarbonate in our lab goggles are more committed to achieving comfort and pleasure in life. The best ways to classify synthetic polymers is by the chemical processes used to produce them; addition polymerization and condensation polymerization. Generally, three important reactions take place in addition polymerization: initiation (birth), propagation (growth), and termination (death). Addition polymers, commonly known as chain growth polymers, are made through a chain reaction in which an alkene monomer is incorporated into the growing chain by reacting with a reactive intermediate. This intermediate is produced by the initiator, which can be a radical (highly reactive atom with an unpaired electron) such as the Benzoyl peroxide that will be used in this experiment. The polymer chain growth takes place during the propagation stage and stops when the radicals are satiated, usually by the recombination of two growing chains. The three different types of polymers are homopolymers, alternating co-polymers and random co-polymers. Homopolymers are made up of the same monomers while alternating co-polymers are made up of two or more alternating monomers and random co-polymers are made up of two or more monomers that follow no particular order (i.e. random). Now condensation polymers, commonly known as step-growth polymers, are formed when two monomers combine to eliminate a small molecule side product, such as water. A unique property of linear polymers is that they cannot form…

    • 3697 Words
    • 16 Pages
    Powerful Essays
  • Good Essays

    Activated Carbon

    • 858 Words
    • 4 Pages

    Activated carbon has the unique ability to adsorb a wide range of compounds from both the liquid and gas phase. This adsorptive feature is responsible for removing contaminants from water and other substances where the adsorbent material is added. Activated Carbon features a highly crystalline form with a wide surface area and extensively developed internal pore structure. Surface area is used as a primary indicator of the activity level, based on the principle that the greater the surface area, the higher the number of adsorptive sites available. Application of high temperatures in the presence of a controlled flow of steam used as the oxidizing medium is what “activates” carbon and produces pore structure. Pore size distribution defines the performance of the material. It is defined as follows:…

    • 858 Words
    • 4 Pages
    Good Essays
  • Better Essays

    for vehicles has tremendously increased. In this scenario, we strongly need an efficient way to control the increasing air pollution led by the exhaust gases from the vehicles. These exhaust gases contains carbon monoxide (CO) and hydrocarbons in high proportions which adversely increases the Global Warming and Green House Effect. The goal of this paper is to introduce a method which adsorbs the hydrocarbons and absorbs carbon monoxide led by the vehicles thereby controlling the Global Warming and Green House Effect. The absorption of carbon monoxide is done by using cuprous salt and adsorption of hydrocarbons is done by using a complex nanomaterial. i.e., Carbon Monolithic Aero gels. Using cuprous salt for absorption of carbon monoxide is no more an innovative idea. But in today’s world of Nano Technology usage of Aero gels (Nanomaterial) to adsorb Hydrocarbons needs a major concern. So in this paper we highlight the production, usage and regeneration of Carbon Monolithic Aero gels.…

    • 1451 Words
    • 6 Pages
    Better Essays