(BAT) Reference Document for the Production of Chlor-alkali ...
(BAT) Reference Document for the Production of Chlor-alkali ... (BAT) Reference Document for the Production of Chlor-alkali ...
Chapter 4 Loading area hazards Fire due to chlorine/iron reaction Fire due to contaminants (oil, organics) Internal corrosion Collision with other rail/road tanks Rupture of the filling pipe Other causes: - Liquid chlorine in vent - Back-flow of chlorine into padding gas system - Valve leaks Examples of preventative measures Use of appropriate materials Avoidance of “hot work” areas No flammable liquids or materials in the surroundings of loading areas -Prohibition of use of hydrocarbon oils, greases and solvents - Use of oil-free compressors in padding gas systems Moisture control system in chlorine and avoidance of possible back-flow Monitoring procedures for wet ferric chloride in valves Braking the transport vehicle and blocking the road or railway track during loading Prevention of runaway rail wagons or tankers getting into filling area Alarms linked to rail retarders -Containment of the loading installation Use of articulated arms or correctly specified flexible hoses and coils for chlorine transfer Maintenance and inspection procedures - Control procedures on gas supplies system to avoid over-pressurisation due to warming - Avoidance of possibility of inversion on the connection between liquid and gaseous phases Examples of corrective or emergency measures Emergency shut off valves on tank and supply initiated by push buttons Emergency shut-off valves Connection of dissipated chlorine gas from the transport vehicle to the chlorine destruction unit - Liquid chlorine in vent detector (alarm/trip) to alert operator - Increasing venting rate and draining liquid to vented tanks - High and low pressure alarms on padding gas system - Padding gas chlorine detector and differential pressure control WORKING DRAFT IN PROGRESS In the storage area Some standard safety measures to achieve optimum risk reduction in the storage area are: Chlorine detection and location and rapid isolation of sources feeding a leak Availability of at least one empty tank of sufficient capacity as an emergency spare 220 December 2011 TB/EIPPCB/CAK_Draft_1
Chapter 4 Good pipework design to minimise the length of pipeline containing liquid chlorine Limitation of the overall liquid chlorine inventory to what is really needed. A simplified layout and a reduction in the number of valves, pipes and connections reduce the risk of leakage For large storage capacities, low-temperature storage at -34 °C is recommended Table 4.19: List of some preventative and corrective or emergency measures to avoid accidents associated with storage of liquid chlorine Storage tank hazards - Vessel failure due to over pressurisation (vapour padding/ inert, liquid overfill) - Internal explosion due to build up of NCl3 - Internal explosion due to hydrogen - Contamination with organics - Contamination with oil Examples of preventative measures - Physical tank protection against over-pressurisation or hydraulic overfill - Maintain stock tank pressure below the maximum allowable pressure - Pump maximum discharge pressure less than maximum allowable system pressure - Design standards of pump, pipework and vessels - Never allow liquid chlorine to evaporate completely to dryness; no branches or wells at bottom of small tanks; brine quality control - No direct connection between a chlorine storage tank and a chlorine gas stream containing hydrogen - Prohibition of use of solvents or organic drying agents - Prohibition of use of oil or hydrocarbon greases, use of oilfree compressors in padding gas system - Use of appropriate materials - Avoidance of “hot work” areas - No flammable liquids or materials in the surroundings of loading areas Examples of corrective or emergency measures - High-pressure alarms on stock tanks - Two independent level/weight alarms on receiving tank - Relief valves at appropriate settings and capacities. It includes, in series: a bursting disk protecting the valve from corrosion; a detection device giving an alarm in case of failure of the disk; a protection against corrosion due to back-flow of moisture from the absorption unit. A protective membrane may be used, or a continuous flow of inert dry gas may be added after the valve. - Pump trips at high level and/or pressure - Pump can be tripped remotely WORKING DRAFT IN PROGRESS - Fire due to chlorine/iron reaction - Corrosion due to chlorine/water reaction; internal corrosion - Check tare weight of tank - Moisture control system and avoidance of possible back-flow - Alarm on padding gas moisture indicator - Response by process operators to evidence of ferric chloride - Chlorine monitors on cooling waterside of heat exchangers TB/EIPPCB/CAK_Draft_1 December 2011 221
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Chapter 4<br />
Loading area hazards<br />
Fire due to chlorine/iron<br />
reaction<br />
Fire due to contaminants (oil,<br />
organics)<br />
Internal corrosion<br />
Collision with o<strong>the</strong>r rail/road<br />
tanks<br />
Rupture <strong>of</strong> <strong>the</strong> filling pipe<br />
O<strong>the</strong>r causes:<br />
- Liquid chlorine in vent<br />
- Back-flow <strong>of</strong> chlorine<br />
into padding gas system<br />
- Valve leaks<br />
Examples <strong>of</strong> preventative<br />
measures<br />
Use <strong>of</strong> appropriate<br />
materials<br />
Avoidance <strong>of</strong> “hot work”<br />
areas<br />
No flammable liquids or<br />
materials in <strong>the</strong><br />
surroundings <strong>of</strong> loading<br />
areas<br />
-Prohibition <strong>of</strong> use <strong>of</strong><br />
hydrocarbon oils, greases<br />
and solvents<br />
- Use <strong>of</strong> oil-free<br />
compressors in padding<br />
gas systems<br />
Moisture control system<br />
in chlorine and<br />
avoidance <strong>of</strong> possible<br />
back-flow<br />
Monitoring procedures<br />
<strong>for</strong> wet ferric chloride in<br />
valves<br />
Braking <strong>the</strong> transport<br />
vehicle and blocking <strong>the</strong><br />
road or railway track<br />
during loading<br />
Prevention <strong>of</strong> runaway<br />
rail wagons or tankers<br />
getting into filling area<br />
Alarms linked to rail<br />
retarders<br />
-Containment <strong>of</strong> <strong>the</strong><br />
loading installation<br />
Use <strong>of</strong> articulated arms<br />
or correctly specified<br />
flexible hoses and coils<br />
<strong>for</strong> chlorine transfer<br />
Maintenance and<br />
inspection procedures<br />
- Control procedures on<br />
gas supplies system to<br />
avoid over-pressurisation<br />
due to warming<br />
- Avoidance <strong>of</strong><br />
possibility <strong>of</strong> inversion<br />
on <strong>the</strong> connection<br />
between liquid and<br />
gaseous phases<br />
Examples <strong>of</strong> corrective or<br />
emergency measures<br />
Emergency shut <strong>of</strong>f<br />
valves on tank and<br />
supply initiated by push<br />
buttons<br />
Emergency shut-<strong>of</strong>f<br />
valves<br />
Connection <strong>of</strong> dissipated<br />
chlorine gas from <strong>the</strong><br />
transport vehicle to <strong>the</strong><br />
chlorine destruction unit<br />
- Liquid chlorine in vent<br />
detector (alarm/trip) to<br />
alert operator<br />
- Increasing venting rate<br />
and draining liquid to<br />
vented tanks<br />
- High and low pressure<br />
alarms on padding gas<br />
system<br />
- Padding gas chlorine<br />
detector and differential<br />
pressure control<br />
WORKING DRAFT IN PROGRESS<br />
In <strong>the</strong> storage area<br />
Some standard safety measures to achieve optimum risk reduction in <strong>the</strong> storage area<br />
are:<br />
<strong>Chlor</strong>ine detection and location and rapid isolation <strong>of</strong> sources feeding a leak<br />
Availability <strong>of</strong> at least one empty tank <strong>of</strong> sufficient capacity as an emergency spare<br />
220 December 2011 TB/EIPPCB/CAK_Draft_1