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8/13/2019 Static Electricity and Cleaning of Equipment (36-40)
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STATIC ELECTRICITY AND
CLEANING OF EQUIPMENT
Presented by:
Dhairya MehtaShamel Merchant
Shashank Maindarkar
Manish Medar
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OVERVIEW
What is Static Electricity
Major Sources in Industry
Some Calculations for Spark Ignition
Minimum Ignition Energy
Hazard Assessment
Precautions to be taken
Case Study
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What is Static Electricity?
Electrical Imbalance on the surface of amaterial
Transfer of Electrons
Causes Spark ignition, which underfavorable (?) conditions can lead to
explosion
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Major Sources of Static in Industry
Use of Power / Conveyor belts
Pulverized materials / dusts
pneumatically transported
The flow of fluids through pipes orconduits, or from orifices into tanks or
containers
The flow of gases from orifices The use of rubber-tyred vehicles
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Typical NumbersCharge production in typical operations for non-
accumulators[C/kg]:
Non-Accumulators: Conductivity < 50 pico - mhos/cm
Sieving: 10-11
- 10-9
Pouring: 10
-9
- 10
-7
Micronising: 10-7
- 10-4
Pneumatic Transport: 10-6
- 10-4
Calculation example:Pouring operation of 100 kg Product: (10-8C/kg)Charge on product: 10-6CSpark energy: E = 0.5 x C x VC = 10-6 C; V = 10 kV (typical value for spark discharge) Thendischarge energy
E = 5 mJ 5
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Minimum Ignition Energy
n
ergy
or
gn
on
Concentration (v.p; temp)
Min (oxygen)
Min (air)
MIE the minimum energy that can
ignite a mixture of a specified
flammable material with air or
oxygen, measured by a standard
procedure
Typical minimum ignition energyvalues for Combustible Vapors:
Soot: > 4000 mJ
Natural products: > 10 mJ
Organic chemicals: 1-10 mJAluminium, Sulphur: < 1mJ
Methane: 0.3 mJ
Carbon disulphide: 0.068 mJ
Hydrogen: 0.012 mJ
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Electrostatic Hazard Assessment - logic
Is there a flammable atmosphere?
Will charge be generated?
Can charge accumulate?
Is the field strength high enough tobreakdown the surrounding air?
Is there sufficient energy to ignite the
flammable atmospheredischarge type?
If the answer is YES, then there is a risk of
ignition!
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General Means of Control
Bonding and earthing of stationaryconductive equipment.
Increasing the conductance of floors,
footwear, wheels and tyres Increasing the conductivity of non-
conductors
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Fig. Filling a Tanker with a Flammable Liquid
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PrecautionsMINIMISE CHARGING
Fluids
Keep Flow Velocity Low
Avoid 2ndPhase entrainment
Avoid Pumps, Filters etc. specially near vessels
AVOID CHARGE ACCUMULATIONEarth All Conducting Parts - e.g. plant & items
oGenerally
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Barton Solvents Wichita facility
Case - Study Flammable Liquid: VM & P Naphtha
Incident:While Transferring VM & P
Naphtha to a storage tank, an explosion
occurred. (July, 2007) Investigated by: U.S. Chemical Safety and
Hazard Investigation Board
Main Cause: Static Electricity SparkIgnition
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Key Findings
Tank Contained ignitable vapor-air mixture in the head space
Stop-start filling, trapping air in the transfer piping
The tank had a liquid level gauging system float with a loose
linkage
The MSDS for the VM&P naphtha involved in this incident did
not adequately communicate the explosive hazard. 12
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Recommendations
Add a Nonflammable, Nonreactive (inert)gas to tank head Space
Modify or Replace Loose Linkage tank
level floats Use Anti-Static Additives
Reduced flow (Pumping) Velocity
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CLEANING OF EQUIPMENT IN
PROCESS INDUSTRIES Main methods:
1. Chemical
2. Mechanical
3. Combination of chemical and
mechanical
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Chemical cleaning to remove
Deposits build up due to:
1. Carbonaceous or organic structuremolecules
2. Algae and slime organisms
3.Degradation deposits
4. Preoperational deposits
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CHEMICAL CLEANING SOLVENTS
Alkaline Cleaners- Degreasing of metal surface
- Caustic Soda-Surfactant
- Caustic Soda plus potassium permanganate (for sulfide
deposits)
Organic Acids
- Remove oxides, mill scale and other impurities
- Monoammoniated Citric Acid
Citric IonChelating agent for iron (pH 3.5)
Inorganic Acids
- Remove water side deposits, iron oxides and calcium
scales- Inhibited Muriatic Acid HCl Inhibited Sul huric Acid
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CHEMICAL CLEANING SOLVENTS
Organic Solvents
- Removal of grease and oil spots
- Spent solution might be recyclable
- M-Pyrol for PVC Reactors Complexing, chelating or sequestering agents
- React with hardness ions, forming water soluble
complexes
- Expensive but selective complexation
- Ease and safety
- EDTA, gluconates and polyphosphonates
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Solvent Cleaning Methods
Circulation- Circulation of solvent
Cascade Method
- Used for towers- Chemical pumped through reflux lineand cascade down over trays and interiortower
- Soils at bottom of trayunremoved
- High pumping capacity of solvents
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Solvent Cleaning Methods
Fill and Soak- Vessel filled with solvent and let to soak
- 15 min1 hour
- Proper flushing to remove loose soil
- Ventto remove gases produced during reaction between soil and
deposit On stream Cleaning
- Steam Vapor phase cleaningsolvents introduced at highpressure, soils carried with vapor
- Foam CleaningFoamed solvent solution to increase contact time
- Foam also has characteristic property of reducing static electricity- Cost effective compared to fill and soak
- Aeration reduces total weightimportant when structuralintegrity ?
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Solvent Cleaning Methods
Gel Cleaning- Similar to foam cleaning
- Gel type cleaning agent sprayed orbrushed on surface
- Remove iron oxide prior to painting- Eg. naval gel
Pickling and passivating
- Agents act as corrosion inhibitors andpassivators
- CS use HCl, Alloy use ammoniated citricacids
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Mechanical Methods
Water jetting- Hyperblasting water used at 1000-10000 psi
- Sheer force remove deposits
- Consists of lances and specially designed nozzle
- Extremely dangerous
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Mechanical Methods
Hydrodrilling, Plugs, Crawlers
- Special drills used with water to cut
through heavy deposits in tube walls
- WaterLubricant and flushing
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Case Studies
Xerox
670000 pounds of emissions
Replacement of chlorinated solvents with
citric acid
Reduction of emissions by 90%
Saves USD 40000/yr in hazardous waste
disposal
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Case Studies
DuPont-Merck
Installed integrated ultrasonic transducer
and rod-shaped tubular ultrasonic
resonator Eliminates the need to buy cleaning
solvents and to dispose of solvent waste
Vapor emissions on site were reduced by80%
8 cleaning cycles to pay for the system
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Case Studies
Parr Paints
Installed high pressure system
Reduction in latex adhering to walls
Cost of high pressure unit, $800.
Savings in waste disposal, $3000/yr.
Payback, 1.7 months
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THANK YOU
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