Brief Introduction To Induced Symbiotic Osmosis Processes for Saline Fluids Desalination and Power Generation

Transcription

1 Brief Introduction To Induced Symbiotic Osmosis rocesses for Saline Fluids Desalination and ower Generation Austin resentation- September 2016 MIK Technology Harnessing The otential Of Renewable Resources For Sustaining Life. 9/22/2016 1

2 1. Brief introduction of the company: MIK Technology Brief Introduction to Induced Symbiotic Osmosis rocesses for Saline Fluids Desalination and ower Generation MIK Technology is a small emerging company with emphasis on developing technologies for harnessing the potential of renewable resources for sustaining life. 2. Technical description of the Technology: Maximizing the potential of using earth renewable resources, particularly water and solar energy, to mitigate the devastating impact of global warming due to the overwhelming increase in world population and subsequent increase in the consumption of fossil fuels; 3. Description of its intended application/market segment; Worldwide applications, anywhere carbon based energy sources can be replaced. 4. Description of I and how it is protected; All technologies are patented or patent pending by USTO or atent Treaty Corporation (CT). 5. Concise business plan identifying how it is planned to go to market (channels to market, partnering/licensing plans, funding needs, etc.); The proposed projects are massive. Cooperation or affiliation with governments and large corporations is necessary. Note: a List of atented and atent ending Technologies is included on last page, 9/22/2016 2

3 MIK TECHNOLOGY INTELLECTUAL ROERTY- ALTERATION OR MODIFICATION OF THIS COYRIGHTED DOCUMENT IS STRICTLY ROHIBITED AND ROTECTED BY UNITED STATES COYRIGHT LAWS ALL RIGHTS RESERVED 1.0 m 3 /s, 7%C 1.0m 3 /s,< 100 ppm m 3 /s, 10.5 %C 0.667m 3 /s, 1.333m 3 /s,< 100 ppm C = 7% C = 5.25% C=5.25% CV >784~1000+ psi ~ 0.0 % CV >588~735+ psi CV >588~735+ psi SWRO Module SWRO Module SRO CELL Tie Line m 3 /s Tie Line m 3 /s O 560 SI LMCD = LMCD = LMCD = Os 784 SI ~ 0.0 % Os 588 SI Os 588 SI 2.0 m 3 /s, SW3.5%C C = 3.5% FIG 1a: Conventional seawater reverse osmosis module for 50% water recovery. C = 1.75% 2.0 m 3 /s, SW 3.5%C 2.0 m 3 /s 1.75%C FIG 1b: Seawater symbiotic reverse osmosis [SRO] train of one SWRO module and SRO cell for 67% water recovery. C = 1.75% FIG 1a,b: The Concept of Seawater Symbiotic Reverse Osmosis [SRO] Desalination 1 m 3 /s = US gal/s is used as a criterion for design. Other smaller units (liter or cubic foot /sec can be also used) 9/22/2016 3

4 Brackish Brackish Saline Desalinated otable Saline Desalinated otable X ressure Exchanger, Hydraulic Turbine, Relief Valve Symbiotic Reverse Osmosis [SRO] rocess Inventor: Maher I. Kelada 3 m 3 /s C = 4% 1.5m 3 /s 1.5 m 3 /s C = 4% C = 4% X f X f X 1 4% SWRO Desalinated Flow 3 m 3 /s 3 m 3 /s Tie-line 4.5 m 3 /s 8% SWRO 4% SRO Cell LMCD = m 3 /s 2% 2% 1.0% F 6 m 3 /s M 1 C = 2% C = 1% C = 1% FIG 2a: 2% Brackish Desalination for 50% Recovery at Differential Salinity Concentration of 4% (Os = 448 SI) with One RO Module F 6 m 3 /s M m 3 /s M 2 FIG 2b: 2% Brackish Desalination for 75% Recovery at Differential Salinity Concentration of 4% (Os = 448 SI) with One SRO Cell FIG 2a, b: Single Cell [SRO] 2% Brackish 75% Recovery. Number of stages may increase in case of increasing flow recovery, while increasing rejected brine salinity. MIK TECHNOLOGY INTELLECTUAL ROERTY- ALTERATION OR MODIFICATION OF THIS COYRIGHTED DOCUMENT IS STRICTLY ROHIBITED AND ROTECTED BY UNITED STATES COYRIGHT LAWS ALL RIGHTS RESERVED 9/22/2016 4

5 Drain: ~0% 3.5% C 3.5% C 1m 3 7% Energy Estimation ISO Cell MJ ISO CELL MJ otential energy generation Total pumping energy Membranes LMCD: Net energy generation: (NE) System efficiency NE/E NE/m 3 of brine feed 6.95 MJ MJ 2.53, MJ 10% 0.7 MJ M 1 M mega joule = 0.7KW/ % salinity range MJ 2.34 MJ T 1.75% C 1.75% C 4.61 MJ T Four Cell Train at 14% C = 3.8KW/liter-sec, Great Salt Lake ISO ower at 24% C = 16KW/liter-sec, Qattara, Egypt ISO ower at 31% C = 20KW/liter-sec, Mauritania, ISO ower at 32% C = 25KW/liter-sec 1m 3 /s@ ~0% 2 m % 2 m 3 3.5% FIG 3: ISO ower Cycle Simulation MIK TECHNOLOGY INTELLECTUAL ROERTY- ALTERATION OR MODIFICATION OF THIS COYRIGHTED DOCUMENT IS STRICTLY ROHIBITED AND ROTECTED BY UNITED STATES COYRIGHT LAWS ALL RIGHTS RESERVED 9/22/2016 5

6 Low Salinity Side Saline Evaporation ond Induced Symbiotic Osmosis [ISO] for Salinity ower Generation Inventor: Maher I. Kelada Cell High Concentration Operating Line, HCOL > 30 % Tie-line Cell 1 Cell 2 Cell 3 Cell n p0 p1>p0 p2 >p1 p3 >p2 pn >pn-1 > 0 % Cell Low Concentration Operating Line, LCOL < 8 % FIG 4: Four ISO ower Cycles For Hypersalinity Simulation MIK TECHNOLOGY INTELLECTUAL ROERTY- ALTERATION OR MODIFICATION OF THIS COYRIGHTED DOCUMENT IS STRICTLY ROHIBITED AND ROTECTED BY UNITED STATES COYRIGHT LAWS ALL RIGHTS RESERVED 9/22/2016 6

7 MIK Technology List of atented and atent pending Technologies 2.1 Induced Symbiotic Osmosis [ISO] For ower Generation, 2.2 Symbiotic Reverse Osmosis [SRO] For Maximizing And Salts Recovery From Saline s and Brines, 2.3 Methods Of Making Flat Sheet Membrane Element [FSM], 2.4 Hollow Fiber Membrane Elements [HFM] And Methods For Making Same, 2.5 Symbiotic Fluids Fractionation And Osmotic rocess By Flat Sheet Membrane anels, 2.6 Symbiotic Reverse Osmosis For Maximizing Desalinated Recover From Saline s and Brines, 2.7 Ecologically Sustainable Hydraulic Fracturing [ES-FRAC] rocess And Apparatus, 2.8 V-CS-ISO &ORC Solar Renewable Energy For Day/Night Operation In Harsh Environment, 2.9 Miscellaneous atented Technologies; Countertop Flow Board urification, Waste Sequential Dissolved Air Flotation Cascade Ion Exchange Columnar Deionization Systems 2.10 Renewable Chemistry Technologies For Bio-agro Chemicals For Manufacturing Fertilizers MIK TECHNOLOGY INTELLECTUAL ROERTY BREIF- All TOICS ARE ATENTED OR ATENT ENDING AND ROTECTED BY UNITED STATES COYRIGHT LAWS ALL RIGHTS RESERVED 9/22/2016 7