DOE_MaxR
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Transcript of DOE_MaxR
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MMAXAXRRTMTM
TTrreaeatmenttment PrProcessocessMaximum Removal of Soluble Species Using
Physical Chemical Treatment
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What is MaxR... Improved Process Treatment Technology
Maximum Rate (Dewatering)
Maximum Reaction Rate
Maximum Reaction Efficiency
Maximum Reaction Stability
Maximum Reduction of sludgevolume/mass
Let the MaxR System Work for You
Maximum Results
Maximum Recovery
Maximum Removal
Maximum Rho ( density)
Maximum Return of CapitalInvestment
Conventional Treatment
The standard method by which dissolved metals and
other soluble species involves addition of reagents into theprocess stream to drive precipitation and form solids. Solids
precipitated in this manner form very finely divided particles
which settle slowly, forming a low density sludge that is
difficult to dewater.
MaxR Process Treatment Technology
The MaxR Process improves on this basic process by using
recycled thickener underflow to serve as precipitation sitesfor fresh solids. Underflow solids are recycled and mixed
with incoming feed reducing chemicals required. Newly
precipitated solids grow on top of existing particles forming
large crystals that settle rapidly to a higher final density.
The ultimate discharge slurry density of a material
(solids concentration) can be increased by 5-30 wt% over
conventional treatment. In addition, if mechanical dewatering
is used, the dewatering rate is greatly increased due to the
high density of the feed sludge and improved dewatering
characteristics of the solids. Subsequently the size and the
cost of the dewatering equipment are reduced.
Equipment Required for Conventional Treatment Flow
Equipment Required forMaxR Process Treatment Technology
Sludge Disposal /Transport
PolishFiltration
Precipitation
Precipitation
Sedimentation
SludgeFiltration
Chemical(s)
SludgeDisposal /Transport
PolishFiltration
Precipitation
Precipitation
Sedimentation
SludgeFiltration
Chemical(s)
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MaxR System Optimization and Dorr-Oliver Eimco Equipment
3
E-CAT
ClarifierDeep Cone Paste
Thickeners
Granular Media Filters(OTG, SVG, VPF,
SBWFilter Styles)
Reactor-Clarifier UnitConvention Clarifier withE-DUC Feedwell
Oxallizer
Oxidation Reactor
Reaction Vessels
Sludge Disposal
Effluent Discharge
Shriver Filter PressRotary Vacuum Filters(EIMCOBeltRVF)
Dorr-Oliver Eimco HorizontalBelt Vacuum Filter
SBW
Filtration Process
Sedimentation Process
Final Filtration
Vertical PressureFilter VPF
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Complete Turnkey Responsibility
Dorr-Oliver Eimco has been a
leader in the manufacture of
process equipment for the past 50
years. We have successfully
integrated this significant process
expertise into the service of
providing complete project and
process responsibility. Specifically,
we can offer the following:
Bench Scale Testing
Pilot Scale Testing (On-site or at our facility)
Flow Sheet Development and Optimization
Equipment Sizing and Integration
Equipment Supply
Detail Engineering
Construction Management
Start-up and Operator training
Continued Parts / Service Department
COMPLETE Process System Design and Control
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Complete Project and Process Responsibility
The MaxR Treatment Process can be applied in any
application where chemical precipitation occurs and where
the process can be modified to control the reaction process.
Applications where Dorr-Oliver Eimco has obtained process
improvement include:
Magnesium Hydroxide Production
Acid Mine Drainage (Metal Hydroxides and CaSO4)
Steel Mill Acid Pickle (FeCl3, HCl)
Water Softening [Ca(HCO3)2, Mg(HCO3)2, SiO2]
Rare Earth Oxide Production (Lead Sulfide)
Chemical Plant Wastewater (Calcium Fluoride)
Agra-Fuel Ethanol Production (CaSO4, Metal Oxides)
Phosphate Wastewater Treatment [CaF2, CaSO4, Ca(PO4)3]
Mineral Sands Beneficiation (Iron Hydroxide and CaSO4)
Brine Treatment in Caustic Chlorine and Food
Applications (CaCO3)
Mineral Leaching Solution Treatment
(Metal Oxides and CaSO4)
Ground Water Treatment in Natural Gas Field
(Barium Sulfate)
Typical Applications
Ground Water Treatment
(Calcium Carbonate, Fluoride and Boron)
Titanium Dioxide Wastewater Treatment
(Iron/Metal Hydroxides/Calicum Sulfate)
Industrial Wastewater from Latex Manufacture
(Magnesium Hydroxide)
Fluoro-Hydrocarbon Manufacture Wastewater
(Calcium Fluoride & Arsenic)
Aluminum Reduction Facility Wet Scrubber
(Calcium Fluoride and Sulfate)
Power Plant Wastewater (Metal Selenium Sulfites)
MaxR Process Portable Pilot Unit
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Caustic-Chlorine/Brine Treatment
Dorr-Oliver Eimco has successfully applied the MaxR
Process for use in brine treatment, where removal of soluble
magnesium, silica, and other metals as precipitated solids is
required. Several installations have enabled us to demonstrate
the MaxR Process performance in saturated brine applica-
tions. Specifically at the most recent installation in Louisiana,
we had the opportunity to compare the MaxR Process
versus a Conventional Treatment System that has yet to be
upgraded to a MaxR Process. MaxR treatment technology
generated superior effluent quality, produced a more dense
sludge, and reduced the quantity of chemicals required.
Effluent Comparison (Settling Time = 5 minutes)
MaxRProcess requires less excess chemicals to achieve
same removal of a soluble species. Shown, in the chart to the
left, is the calcium removal versus excess carbonate required
in brine treatment.
The MaxR Treatment Process
Dramatically Improves Brine Treatment Performance
Maximize treatment capacity with minimized
capital/operating costs
No External Reaction Tanks Required
Reduced Sludge Filter Size
Maximizes Savings in Sludge Disposal Costs
Filter cake solids increases from 15-40 wt% to 40-70 wt%
Maximizes Dewatering Equipment Performance
Clarifier loading increases from 0.5 m/hr to 1.5 m/hr
Clarifier Underflow solids increase from 3-10 wt% to 15-40 wt%
Filtration rate increases by 3X-20X compared to Conventional
Treatment Processes
Maximizes Utilization of Chemical Additives. Reactant Chemical Consumption is Reduced by 5-25%
Excess Chemical Concentrations Reduced by 25-50%
Excess Na2CO3 400-600 ppm
Excess NaOH 150-300 ppm
Maximizes System Chemical Stability
Maximizes Metals Removal Producing Lower Effluent
Concentration
Soluble Calcium from clarifier 0.45-1.25ppm
Soluble Magnesium from clarifier 0.025-0.04ppm
Soluble Silica reduce to less than 3 ppm as SiO2
Soluble Calicum vs. Excess Carbonate Required
Typical MaxR
Brine Treatment Process Flowsheet
VacuumFilter
GranularMedia Filter(Anthracite)
VerticalPressure
Filter
Filter Press
Reactor Clarifier Unit
FilterCake
FilterCake
Filtrate
SludgeRecirculation
Raw UntreatedBrine Influent
TreatedEffluent
Polymer
Na2CO3 AdditionNaOH Addition
Thickener SludgeDischarge to Filter
Finished Brine
ConventionalTreatment
MaxR
Process Treatment
Excess Carbonate (ppm)
200 400 600 800 1000 1200
10
8
6
4
2
0
Ca(ppm) Filter Press
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Applications
Acid Neutralization and Metal Hydroxide
Removal for Water Treatment and Re-use
Virginia
Effluent < 15 NTU
Sludge thickener underflow 30 - 50 wt%
Vacuum filtration solids 70 - 75 wt%
Acid Mine Drainage Treatment
California
Annual operational savings = $1 million
Solids concentration doubled in drying ponds to 65 wt%
Vacuum filtration rate increased by 20X
Center column pumping - no tunnel required
Brine Process Treatment
Louisiana
Silica out < 1 mg/L
Sludge thickener underflow = 40 - 60 wt%
Excess chemicals decrease by 30 - 50%
Water blanket technology utilized
Super-Phosphate Fertilizer
Brazil
Characteristics
Inlet (mg/L) Discharge (mg/L)
SS 20,000 < 200
F 1,300 < 5
PO4 2,500 < 80
Scale formation reduced
Sludge thickener underflow = 25 wt%
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Power Plant Wastewater
Pennsylvania
Provided a complete turnkey project
MaxR Process which includes:
Reactor Clarifier Unit
Thickener
EIMCOBELT RVF and SVG Filters used in conjunction
with our advanced biological/aeration technology,
Advent Integral System
Underflow to vacuum filter is 40 wt%, cake of 65 wt%
Influent SS concentration = 70,000 mg/L, final SS
effluent averages less than 20 mg/L
Steel Mill Wastewater
China
Characteristics
Inlet (mg/L) Discharge (mg/L)
SS 400 < 20
O&G 400 < 5
Zn 80 < 2
Filtration cake >50 wt% solids versus 35 wt% solids
obtained from parallel conventional treatment train
Reference Installation List
State/ Operation Pilot Equipment Process Equipment Tankage/ Construct. Start-Up Operator
Application Country Date Feasibility Plant Sizing Design Supply Erection Mangmnt. Services Training
Process, PbS CA 1984 X X X X X X X X
Brine Treatment (Food Industry) WI 1988 X X X X X X X X
Chemical Plant Wastewater MS 1989 X X X X X X X X
Fertilizer Wastewater Brazil 1991 X E X X X X X
HF Wastewater LA 1992 X X X X X X X X
Hydro-Metallurgical Process UT 1994 X X X X X X X XAcid Wastewater OH 1995 X X X X X X X X
Acid Wastewater OH 1996 X X X X X X
Fertilizer Wastewater Thailand 1997 X E X X
Acid Mine Drainage CA 1997 X X X X X X X X X
Acid/Alkali Wastewater China 1997 X X X X X X
Mine Water Infiltration NV 1997 X X X X X X X X
NaOH-CI2 Brine Treatment LA 2000 X X X X X X X X
Power Plant Wastewater PA 2000 X X X X X X X X
NaOH-CI2 Brine Treatment LA 2001 X X X X X X X X
NaOH-CI2 Brine Treatment KY 2001 X E X X X X X X
TiO2 Acid Neutralization VA 2002 X E X X X X X X X
E = Pilot testing results obtained from Experience/Testing from previous similar projects
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Dorr-Oliver Eimco is here to help you with all your solid/liquid separation needs. Please call us to
find out more about how Dorr-Oliver Eimco technology can improve your productivity. In the U.S.,
please call 1.801.526.2000 and in Canada, call 1.705.325.6181.
Copyright 2006 Dorr-Oliver Eimco. All rights reserved. Eimco, Dorr-Oliver & various
marks used are proprietary/registered trademarks of GL&V and Dorr-Oliver Eimco.
Global Sales, Service and Full Equipment Life Cycle Support
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