Separation of Oil from Water TEAM H 2 OLEUM Ali HasanMahdi Mohammad Christina HoltDaniel Pardo April 24, 2015.

Slides:



Advertisements
Similar presentations
DAF Whitewater Systems
Advertisements

CE Lab Jar Test.
Importance of Effective Sand Management - DTI View Colin Cranfield Reservoir Engineer Licensing & Consents Unit, Aberdeen.
 Ongoing energy crisis  Depletion of fossil fuels  Search for an alternative energy source  Biogas is underutilized  Affordable and can be widely.
CE 370 Sedimentation.
I E Industrial Equipment Servicing the North State Environmental Cleaning Systems Site Design Comparisons Site Design Comparisons (System Pretreatment)
The students in the Freshman Academy & the Green School Initiative are proud to present the following on- line tutorial about biodiesel production at HPHS.
. Abridged Project Methodology 15 th October 2013 Graham Mann.
CE 370 Filtration.
December 2010 Your Natural Microbial Service Provider Efficiency and Cost-Effectiveness.
Oil and Grease in Wastewater ENVE 202 Dr. A. Kerç.
Lecture 4.
Pulse Drying What is it?. Pulse Drying Pulse drying is a relatively new technique for rapidly drying high moisture/medium solids feed streams into a much.
Alabaster Corp. Tank Cleaning and Degassing General Process Overview.
Surface Water Treatment Plant
Antunes Water Filtration Technologies Introduces to You:
ReduDust A System for Bypass dust recovery By: Ing
Dr Saad Al-ShahraniChE 334: Separation Processes Absorption and Stripping of Dilute Mixtures  In absorption (also called gas absorption, gas scrubbing,
BASFORD GAS WORKS REMEDIATION USING SOIL WASHING TECHNOLOGY.
20,000 Barrel Per Day Produced Water Treatment System
Elements/Media t Types t Comparison t Which one do I use? t Construction t Testing.
Facility Design Tutorial This tutorial is designed to enhance knowledge of biotechnological/pharmaceutical processes. The topics covered within this tutorial.
Wednesday, 12/12/2007, FYROM Prevention of Contamination from Mining & Metallurgical Industries in FYROM Strategic Plan for Prevention of Contamination.
ZF-100 The Paraffin & Asphaltene Solution. ZF-100 The Paraffin & Asphaltene Solution 72% Biodegradable, environmentally friendly ZF-100 is an aggressive.
Efficient Pigging of Gathering Lines
Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering WTP Project Safety, Expectations, Economics, Logic Raw water To waste F1F1 F1F1 S1S1.
CHEE 370 Waste Treatment Processes
Unconventional Gas: Shale Gas Shale Gas  Unconventional gas (hydrocarbons) found in subsurface shale formations  Replacement to coal, oil, and natural.
Introduction to Environmental Engineering Code No. (PE389) Lec. 5 and 6.
Water Treatment Stations Tue. (am) Tue. (pm) Wed. (am) Wed. (pm) Thur. (am) Thur. (pm) Station 1Mini-pilot (CO 166 Greenhouse - Liz) Station 2NF.
Fuel Oil Maintenance and Filtration Selection
Demystifying SelfSensing Pumps. Design Operating Point 300 Gallons Per Minute 53 Feet of Head System Curves 150 ton 12deg Delta T 60 GPM each.
IT IS THE PROCESS OF REMOVING IMPURITIES OF RAW WATER TO BRING ITS QUALITY UP TO CERTAIN REQUIRED STANDARDS IS CALLED WATER TREATMENT.
PHOSPHORUS REMOVAL FOR LAGOON OPERATORS WHY THE CONCERN OVER P.
Business Opportunity EPRS Energy Co. Inc.. Overview World-wide oil production has been declining for decades. There are over 400,000 stripper or marginal.
Permanent Housing for a Ceramic Oil Filter MIM U702 Capstone Design reNU Design Team Dale Kochevar Kelly Seitz Marco Solia Barrett Straub Matt Whalen MIM.
Marcellus Shale Wastewaters Management by Resource Recovery Shale Gas Innovation Contest Ben Franklin Technology Partners April 13, 2012 Timothy Keister,
Accelerated Landfill Energy Recover Technology Dr. Te-Yang Soong, PhD, PE CTI and Associates, Inc. Wixom, Michigan.
TEAM 12: Low-Cost, Portable, Off-Grid Biodiesel Production Plant Team Members: James Black Sam Dresser Joey Kilmer Matt Mills Faculty Advisor: Dr. Dave.
1 Waste Treatment, Chemical ENVE Why Treat Waste Have a RCRA Waste –TSDS –Treat instead of disposal, landfill –Treat before disposal Or treat in.
Processing, distribution and use of water.
Wally’s dream job The first process to be done: Wafer Cleaning Wafers must be free of contamination at all stages of the antenna fabrication process.
Wally’s dream job The first process to be done: Wafer Cleaning Wafers must be free of contamination at all stages of the antenna fabrication process.
5.6 SEDIMENTATION Objective
Northern Great Plains Water Consortium (NGPWC) Bakken Water Opportunities Assessment Water Resource Opportunities Meeting Bismarck, ND December 10, 2009.
1 Lake water (raw) Flocculation Flash mix Gentle mix Quiescent condition Sedimentation Precipitation Coagulant.
Considerations and operational challenges in choosing Membrane Filtration for a Water Treatment Plant Upgrade Ed Cross Division Manager, Water Supply and.
Date: Monday, May 11 th 2015 Topic: Water Purification Objective: To recognize the stages of it.
Natural Gas & Propane Raqwan Griffin 3 rd hour. What is Natural Gas Natural Gas is a mixture of hydrocarbons, predominantly, methane, ethane, propane.
Presented By: Aaron Goodwin Mike Pyrkosz April 15, 2004 Aquarium Wave Generator Project # A Design Review.
The Los Angeles Aqueduct Filtration Plant An Overview of Facilities and Operations.
David J. Berestka, PE Remedial Design Engineer, Tetra Tech EM Inc.
SAGD (De-Oiling) Solutions. SAGD Produced Fluid Separation requirements: Sand Removal: continuous, batch process, in tank separators Oil Removal: cyclones,
Game-Changing Technology for Oil Water Separation. The Development of the RJOS High Efficiency Oil Water Separation System Presented by Wade Bozak C.E.T.
Khalid Aldhahri Omar Alrajeh Daniel Marken Thomas White CLEAN AIR POWER ASU with Oxy-fuel Combustion for Zero Emission Energy University of Wyoming College.
Course TEN-702 Industrial waste management unit-2 Lecture -8 & 9.
We use at our unit polymeric membranes to separate hydrocarbons without heating feedstock to the boiling point, and without using fired heaters.
Course TEN-702 Industrial waste management unit-2 Lecture -13.
Integration of Accelerated Precipitation Softening - Microfiltration (APS-MF) Assembly to Maximize Water Recovery from the Treatment of Brackish Water.
Environmental protection
Groundwater Pilot Treatment System Update May 2017
ENVIRONMENTAL PROTECTION External EHS Expert Panel Workshop
Drinking-water Treatment
Electrocoagulation Treatment of Heavy Metals from Mine Impacted Water
Jar Testing of Chemical Dosages
Mohr Separations Research, Inc.
Objectives of Pollution control o Prevention of nuisance o Prevention of physical damage to property o Elimination of health hazards to plant personnel.
Presentation transcript:

Separation of Oil from Water TEAM H 2 OLEUM Ali HasanMahdi Mohammad Christina HoltDaniel Pardo April 24, 2015

Overview  Client description  Problem statement  Needs statement  Preliminary research  Emulsion & Separation  Bench scale emulsion  Overall system  Coagulation & Gas Injection System  Analysis  Project timeline  Budget 2 Mahdi Mohammad

Client Description Waste-Management Education and Research Consortium (WERC)  Typically, the environmental tasks have no known solution or the available solutions do not meet performance criteria 3 Ali Hasan The goal of the competition is to design, develop, and test actual environmental processes for real-world problems.

Problem Statement  Task:  Emulsion techniques  Separate emulsified oil in water  Design:  Cost effective  Efficient  Robust  Ideal solution:  High degree of separation  100% water 0% oil  100% oil 0% water 4 Ali Hasan Non-emulsion Vs. Emulsion

Project Significance 5  Increased use of petroleum creates a need to remove emulsified oil from water before disposal  This project removes oil contaminants from the water  Safer and cheaper to dispose  Recovers oil

Needs Statement  Full Scale Model:  100 GPM  Uses industrial waste oil  Uses brackish water  Bench Scale:  Emulsified vegetable oil  Represents the industrial waste oil in full scale  Environmental Health and Safety (EHS) disposal Given:  10 gallons of emulsified oil-water solution 200 mg/L concentration  Must obtain one gallon of separated water and 8 ml of oil 6 Ali Hasan

Preliminary Research: Emulsion  Physical Emulsion  Shearing Power  Chemical Emulsion  Emulsification Agent  Sound Energy  Sonicator 7 Christina Holt Sonicator

Emulsion Techniques for Bench Scale Vitamix 7500  ~2.2 horsepower motor  120 V or 12 A  23,000 RPM  Can boil water in under 10 minutes  Cost: $500 8 Christina Holt

Preliminary Research: Separation  Physical Separation  Plate Separation  Electrical Separation  Electrocoagulation  Chemical Separation  Coagulation and Flocculation  Gas Injection System 9 Christina Holt Physical Separation Electrical Separation

Overall System 10 Gas Injection Tanks Coagulation & Flocculation Chemical Injection Storage Tank Mahdi Mohammad

Storage Tank  16,000 gallon storage tank will accommodate flows up to 130GPM for 2 hours. 11 Mahdi Mohammad * All the dimensions are in inches

Coagulation and Flocculation System  Best Chemical?  Chemical: Ferric Sulphate  Dose = 30mg/L  Amount: kg/day  0.2 gram every second 12 Mahdi Mohammad

Coagulation and Flocculation System 13 Mahdi Mohammad Dry Chemical Injection Coagulation & Flocculation * All the dimensions are in inches

Gas Injection System 14 Daniel Pardo  3 gas injection tanks : 1 coagulation system  When 3rd tank is ½ full, 1st tank ready for more emulsion

Gas Injection Tank 15 Daniel Pardo Multiple Gas Spargers Water Exit Oil Exit Valve * All the dimensions are in inches  Compressed Nitrogen Gas  Small Bubble Size  Oil Layer (25 mm = 1inch)  Collection

Bench Scale 16 Daniel Pardo Gas Injection Tank Coagulation and Flocculation System  Coagulation  2 minutes rapid  5 minutes slow  Gas Injection  45 Minutes

Competition Results  NMSU Chemical Team  Clean water  No oil found in water sample  Minimum oil recovery  Losses occurred during transfers  7 Teams  Only first and second announced 17 Daniel Pardo

Analysis 18 Daniel Pardo Stage 1: Emulsion Stage 2: Coagulation System Stage 3: Gas Injection System  Head losses  No overflow  Oil particle size  1. Emulsion Stage  2. Coagulation  3. Gas Injection  Confirms oil will separate

Project Timeline  Research (Emulsion & Separation)  Design Choice  Coagulation System  Gas Injection System  Bench Scale  Final System Full Scale  WERC Competition  Website  Visit our website for more information  Search Keywords: “OilFromWater h2oleum” 19 Daniel Pardo

Budget 20 Christina Holt Cost of Raw Materials Labor Cost ($/hour) Total Man Hours Required Total Labor Cost Subtotal Contingency and Allowance (50%) Total Cost to Build Total System Cost to Build $56,230.26$45.001,600$72,000$128,230.26$64,115.13$192, Cost of Ferric Sulfate Cost of Nitrogen Labor Cost for Operator Energy Costs Subtotal Miscellaneous Costs (30%) Operating Cost for 1 Day Operating Costs Per Day $4.00$25.00$1,080$20.00$1,129$338.70$1,467.70

Summary  Client description  Problem statement  Needs statement  Preliminary research  Emulsion & Separation  Bench scale emulsion  Overall system  Coagulation & Gas Injection System  Analysis  Project timeline  Budget 21 Christina Holt

Thank You for Listening Any Questions? 22