This page contains a Flash digital edition of a book.
Technologies for Oil and Gas Produced Water Treatment


Table 2: Applications of Advanced Membrane Filtration Technologies7 Membrane


Separation specifications filtration


Microfiltration >100,000 Da 10–0.1 µm


Ultrafiltration Nanofiltration


10,000–100,000 Da 0.05–5 e-3 µm


1,000–100,000 Da 5 e-3–5 e-4 µm


Bacteria, viruses, suspended solids, etc.


Proteins, starch, viruses,


colloid silica, organics, dyes, fats, paint solids, etc. Starch, sugar, pesticides,


herbicides, divalent ions, organics, BOD, COD, detergents, etc.


Reverse osmosis Salts and lower MWCO Metal ions, acids, sugars, 1 e-4–1 e-5 µm


aqueous salts, dyes, natural resins, monovalent salts, BOD, COD, ions, etc.


Key: BOD = biochemical oxygen demand; COD = chemical oxygen demand; DA = daltons; MWCO = molecular weight cut-off.


Figure 7: A Two-chambered Vertical Induced Gas Flotation System8


Different horizontal induced gas flotation vessels are used in industries with single or multiple chambers or cells (see Figure 6). Vertical induced gas flotation vessels are favourable for offshore platforms because they take up less space (see Figure 7).8


Membrane Filtration


Membranes are widely used in separation processes. The most applicable membrane filtration processes for oilfield produced water are microfiltration, ultrafiltration, nanofiltration and reverse osmosis (see Table 2). Microfiltration is the separation of suspended particles, ultrafiltration is the separation of


Figure 8: Comparison between Crossflow and Vibratory Shear Enhanced Process (VSEP®


) Separation13 Crossflow VSEP


A number of different aerobic and anaerobic biological processes have been used for treating oil- and gasfield produced water.


macromolecules and reverse osmosis is the separation of dissolved and ionic components. Nanofiltration membranes are generally designed to be selective for multivalent rather than univalent ions. Reverse osmosis membranes are designed to reject all species other than water. They are unable to offer a significant barrier to dissolved gases and certain low-molecular-weight organic molecules.4


oil in water that is 2 µm and larger in diameter (see Figure 5). The technology is a multistage adsorption and separation system. An adsorbent medium, the re-usable petroleum adsorbent (RPA®), removes large and small oil droplets. In the process of adsorption, the medium continuously adsorbs the oil emulsions, coalesces and then desorbs them into larger oil droplets. In the recovery chamber, oil droplets desorbed by the medium float to the top in accordance with Stoke’s law.11


Induced gas flotation


Induced gas flotation is a process in which gas flotation is carried out inside a horizontal or vertical vessel to help the separation of the oil.


108


A key technical obstacle to the cost-effective application of membranes in produced water treatment is fouling: the adsorption or accumulation of certain components of produced water on the membrane surface or in the membrane pores eventually causes flux efficiency to decline.12


New Logic Research uses a vibratory shear enhanced process (VSEP®) separation system that employs torsional vibration of the membrane surface.13


The system creates very high shearing energy at the surface and the pores. The result is a reduction of colloidal fouling and polarisation of the membrane (see Figure 8).


EXPLORATION & PRODUCTION – VOLUME 9 ISSUE 2 Oil


Produced water


Oil/water separator


Water SMZ regeneration Air for


Key: MBR = membrane bioreactor; RO = reverse osmosis; SMZ = surface modified zeolite; VPB = vapour phase bioreactor.


feed Air VPB MBR RO system


Treated water


Treated gas


Applications (removal of) Figure 9: Schematic Treatment Plant (Los Alamos National Laboratory)14


Page 1  |  Page 2  |  Page 3  |  Page 4  |  Page 5  |  Page 6  |  Page 7  |  Page 8  |  Page 9  |  Page 10  |  Page 11  |  Page 12  |  Page 13  |  Page 14  |  Page 15  |  Page 16  |  Page 17  |  Page 18  |  Page 19  |  Page 20  |  Page 21  |  Page 22  |  Page 23  |  Page 24  |  Page 25  |  Page 26  |  Page 27  |  Page 28  |  Page 29  |  Page 30  |  Page 31  |  Page 32  |  Page 33  |  Page 34  |  Page 35  |  Page 36  |  Page 37  |  Page 38  |  Page 39  |  Page 40  |  Page 41  |  Page 42  |  Page 43  |  Page 44  |  Page 45  |  Page 46  |  Page 47  |  Page 48  |  Page 49  |  Page 50  |  Page 51  |  Page 52  |  Page 53  |  Page 54  |  Page 55  |  Page 56  |  Page 57  |  Page 58  |  Page 59  |  Page 60  |  Page 61  |  Page 62  |  Page 63  |  Page 64  |  Page 65  |  Page 66  |  Page 67  |  Page 68  |  Page 69  |  Page 70  |  Page 71  |  Page 72  |  Page 73  |  Page 74  |  Page 75  |  Page 76  |  Page 77  |  Page 78  |  Page 79  |  Page 80  |  Page 81  |  Page 82  |  Page 83  |  Page 84  |  Page 85  |  Page 86  |  Page 87  |  Page 88  |  Page 89  |  Page 90  |  Page 91  |  Page 92  |  Page 93  |  Page 94  |  Page 95  |  Page 96  |  Page 97  |  Page 98  |  Page 99  |  Page 100  |  Page 101  |  Page 102  |  Page 103  |  Page 104  |  Page 105  |  Page 106  |  Page 107  |  Page 108  |  Page 109  |  Page 110  |  Page 111  |  Page 112  |  Page 113  |  Page 114  |  Page 115  |  Page 116  |  Page 117  |  Page 118  |  Page 119  |  Page 120  |  Page 121  |  Page 122  |  Page 123  |  Page 124