1 oleum and sulfuric acid pipeline safety maintenance presented by
Transcription
1 oleum and sulfuric acid pipeline safety maintenance presented by
1 OLEUM AND SULFURIC ACID PIPELINE SAFETY MAINTENANCE PRESENTED BY: • Emar Leão • R d i Maçon Rodrigo M 2 PARANAPANEMA - CARAÍBA The Caraiba Metais’ sulfuric acid facility was designed by Natron Engenharia with a initial capacity of 1.870 t/day. t/day. The main porpouse of the facility is to treat the gases from the copper fundition.. fundition 1982:: H2SO 1982 SO44 facility startstart-up up.. Actual production capacity capacity:: 2.475 t/day after debottlenecking debottlenecking.. Caraíba 3 Background 1. The pipeline is in operation since 1993 and occurred one oleum spillage happened in 1998 1998,, one chemical burn accident and one acid spillage to the ground in 2003, 2003, during preventive maintenance. p maintenance. 2. After 2003, 2003, more than 30 preventive interventions inside and outside Caraiba without accidents. accidents. • Two general painting and 15 pipeline sections paintings; paintings; • Five pipeline sections replacements / external area valve relocation;; relocation • Eight pipeline sections inside Caraiba; Caraiba; • Thickness measurement on semester basis and quarterly vegetation cleanness. cleanness. 4 System characteristics: 1- 12,000 meter long pipelines 5 System characteristics: 2- Height differences up to 30 m 1. PROQUIGEL 2. BRASKEM CPL 3. PUMPING STATION CIBRAFERTIL 4. CETREL ACCESS 5. COPPER PUMPING STATION 6. CARAIBA METAIS 7. PUMPING STATION CARAIBA 6 System characteristics: 3- places with difficult access (height and vegetation vegetation)) 7 System characteristics: 4- places with difficult access (Pipe way inside complex) 8 MAIN OBJECTIVE OBJECTIVE:: Pipeline p maintenance jjobs without accidents and environmental events. events. MAIN STAGES STAGES:: • • Job planning planning:: • Caraiba operation, Braskem and clients selling, maintenance, safety and environmental areas has to work t th ; together; together • Client autonomy less than 03 days; days; • Police and environmental agency official notice. notice. Operational procedure: procedure: • • Pipeline drainage and start start--up procedures; procedures; Task risk analysis. analysis. 9 Operational procedure (resumed): 1. Acid transfer interruption interruption;; 2 Pi 2. Pipeline li gravity it drain d i to t storage t t k andd nitrogen tanks it purge;; purge 3. Depressurize and isolate the pipeline section; section; 4. Open drains and collect the residual product with vacuum truck; truck; 5. Maintenance job execution and shut down the pipeline section; section; 6. Pipeline startstart-up and confirm that there are no leaks leaks;; 7. The h pipeline i li is i ready d again i for f acid id transfer. transfer f . 10 Labels isolating Caraíba side Labels and locks isolating the client side 11 Non destructive testing Non destructive testing Non destructive testing Non destructive testing New screws and gasket 12 Task Risk Analysis: Dangers:: Dangers 1 Sulfuric acid 98 1. 98% % and oleum 28 28% %; Risks: Risks: 1. Skin and/or eyes chemical burns burns;; 2. Product spillage; spillage p g ; 3. SO3 inhalation inhalation;; Risks Mitigation (next slide): slide): 13 Skin, eyes and respiratory protection 14 Skin, eyes and respiratory protection 15 Emergency drills: foam over oleum 16 Collecting tray Sodium carbonate Vacuum truck Suction in progress 17 DIPHOTERINE PLASTIC BAG BOARD EYE WASH 500 mL 500 mL PORTABLE DIPHOTERINE 5.000 mL EYE WASH MINI PD MICRO PD 100 mL 200 mL 100 mL 18 30 min after the accident After diphoterine use After 6 hours Next morning 19 04 years latter 04 years latter 20 Task Risk Analysis: Dangers:: Dangers 2 Flammable products and/or heated products in nearby 2. pipelines;; pipelines Ri Risks: Risks k: 1. Explosion Explosion;; 2. Heat burns burns;; Risks Mitigation (next slide): slide): 21 Flammable atmosphere testing anti--heating hut anti Huts anti--heating cloth anti 22 Thermal heat clothes Thermal heat clothes Thermal heat cloths Thermal heat cloths 23 Task Risk Analysis: Dangers:: Dangers 3 Confined area and poisonous animals 3. animals;; Risks: Risks: • Asphyxia and/or poisoning poisoning;; • Poisonous animals stings stings;; Risks Mitigation (next slide): slide): 24 Eg: confined area and/or animals habitats habitats Bees Snakes Mitigation: cleaning, leg protection and boots Mitigation: oxygen measurements; air; exhaust, ladders 25 Task Risk Analysis: Dangers:: Dangers 4 Weather 4. Weather;; Risks: Risks: • Drown e sudden illness illness;; Risk Mitigation (next slide): slide): 26 Normal condition – ducts in both sides Flooded location – vapor formation Normal condition – duct depth Flooded location – vapor formation 27 Task Risk Analysis: Dangers:: Dangers 5 Road proximity, 5. proximity weight lifting machinery; machinery; Risks: Risks: • Vehicle crashes, running overs; overs; • Equipment q p fall; fall; Risk Mitigation (next slide): slide): 28 Automobile crashes Traffic signs; blockage road and police help Pipe p section liftingg Traffic signs; Industrial complex vigilance 29 Pipe ends are isolated to avoid acid droplets Droplets events 30 Cramps to avoid leakages or pipeline drainage Cold connection cramp Hot pipeline drain Pipeline leaks cramps Stanch leakages near the drain Drain containment 31 Example: Job inside Caraiba area 32 Resources are always available Lifting truck Emergency truck Vaccum truck Emergency KIT 33 Fire response team and operators are trained in several emergency situations 34 THE END