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Application Note December 2016 Corrosion Management Cosasco www.cosasco.com [email protected] Controlling Corrosion Upsets in Phosgene Production with Microcor ® Online Systems

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Page 1: Corrosion Management - Corrosion Monitoring-Cosasco · ppliction ote ecemer Corrosion Management Cossco slescosscocom Controlling Corrosion Upsets in Phosgene Production with Microcor®

Application NoteDecember 2016

Corrosion Management

Cosasco ● www.cosasco.com ● [email protected]

Controlling Corrosion Upsets in Phosgene Productionwith Microcor® Online Systems

Page 2: Corrosion Management - Corrosion Monitoring-Cosasco · ppliction ote ecemer Corrosion Management Cossco slescosscocom Controlling Corrosion Upsets in Phosgene Production with Microcor®

Corrosion Management

Cosasco ● www.cosasco.com ● [email protected]

Application NoteDecember 2016

Background

Phosgene is a relatively easily manufactured through highly toxic gas (chemically COCl2) which is not an end product in itself. The gas is used primarily for the production of urethane and Toluene Di Iso-cyanate (T.D.I.). T.D.I. is a product subsequently used in the manufacture of foam for upholstery, car seats and similar. The toxicity of the phosgene means that it is produced as necessary at the facility where it is required for further use, in preference to storing or transporting the highly toxic gas.

Phosgene gas forms highly corrosive hydrochloric acid when hydrated. Microcor® rapid response online corrosion monitoring system and Electrical Resistance (ER) probes provide a very successful and fast responding system for control of corrosion upsets in these systems resulting from any mixing of water and phosgene.

Phosgene Production Process

Chlorine and carbon dioxide gases are passed through a catalyst bed to produce phosgene gas. The exothermic reaction produces a phosgene outlet temperature which is typically around 180°F necessitating an outlet cooler. The heat exchanger reduces the phosgene gas temperature producing liquid phosgene (see Figure 1). On a typical installation 5 or 6 of these systems may be operating in parallel with water as the cooling media in the heat exchangers; any leakage in the exchanger results in mixing of the phosgene and the cooling water producing highly corrosive conditions.

Heat Exchanger Leak Detection

The corrosion rate of carbon steel in dry phosgene is zero. In cooling water alone it is around 5 mpy. However, with phosgene and cooling water mixed by leakage the corrosion rate may exceed 1,000 mpy. At this corrosion rate, a Microcor Wireless/Wired ER system will indicate the leakage within minutes.

The corrosion rate level of 20 mpy is typically set as an alarm level for leakage detection.

CARBONDIOXIDE

CO2

CHLORINECI2

CATALYSTBED

EXOTHERMICREACTION

PHOSGENE

1800F AMBIENT

COOLINGWATER

MATERIAL OFCONSTUCTIONSTAINLESS STEEL

MATERIAL OFCONSTUCTIONCARBON STEEL

HEAT EXCHANGER

MATERIAL OF

STAINLESS STEEL

MATERIAL OF

CARBON STEEL

CARBONDIOXIDE

CO2

CATALYSTBED

EXOTHERMICREACTION

Ambient

HEAT EXCHANGER

COOLINGWATER

PHOSGENE

1800F

CHLORINECI2

Figure 1 Schematic of Phosgene Process

CONSTRUCTION CONSTRUCTION

Page 3: Corrosion Management - Corrosion Monitoring-Cosasco · ppliction ote ecemer Corrosion Management Cossco slescosscocom Controlling Corrosion Upsets in Phosgene Production with Microcor®

Corrosion Management

Cosasco ● www.cosasco.com ● [email protected]

Application NoteDecember 2016

Probe Mounting and Safety

Permissible probe mounting configurations vary from plant to plant. Some regulations permit use of retractable probes with stuffing boxes, while others will only allow fixed flanged connections (see Figure 4). Standard probes of this type have been used in many applications. However in line with our philosophy of providing high integrity equipment, we are now offering probes with double glass seals at the connector end of the probe for this type of lethal service (see Figure 3). As deterioration of the measurement element occurs process fluid may penetrate the interior of the probe. With this design two sets of seals remain between the process and the exterior of the probe. If desired the cavity between these seals may be pressurized with a suitable fluid above process pressure or vented to a safe detection area. Glass seals provide good sealing capability for acidic environments except for hydrofluoric acid (they should not be used for toxic environments with a pH greater than 9.0).

Figure 3 - Double Back Glass Sealed Connector

Figure 2 - Microcor Online Wireless System

Figure 4 - M2520 Microcor Fixed Probe

Page 4: Corrosion Management - Corrosion Monitoring-Cosasco · ppliction ote ecemer Corrosion Management Cossco slescosscocom Controlling Corrosion Upsets in Phosgene Production with Microcor®

Corrosion Management

Cosasco ● www.cosasco.com ● [email protected]

Application NoteDecember 2016

Corrosion Monitoring of System Fed by Phosgene The production plants fed by phosgene, such as urethane and T.D.I. production facilities may well provide greater potential for ER probes than the phosgene plant itself. An existing customer manufacturing T.D.I. at one of the largest USA facilities (production approximately 2 million pounds per year) has two probes on his phosgene plant but a further 25 probes on the T.D.I. production section of the plant.

The plant comprises reactor vessels, distillation columns and heat exchangers. While the reactor vessels are nickel-lined and there are a number of monel pipes but the majority of the plant is carbon steel.

At the front end of the plant the problems derive from corrosive nature of phosgene and other solvents if they become hydrated. Reactor vessels with steam heated jackets present another potential corrosion problem since a leak would permit the higher pressure steam to leak into the reactor causing a highly corrosive condition. Probes positioned in the reactor outlets provide detection for such leaks.

On the distillation columns the outlet streams pass through overhead condensers cooled by water. Generally the process pressure is greater than the cooling water pressure so that any leaks would be into the cooling water. Hence in these cases probes are placed in the cooling water outlet. Alternatively where process side pressures are less than that of the cooling water, the probes would be installed on the process outlet of the exchanger.

In some cases, carbon steel probes are also used in the nickel and monel areas of the plant to provide a fast response to changes in corrosive conditions, provided the conditions are not too severe so that probe life is unacceptably short. In these cases optimization of probe spans may be required.

Page 5: Corrosion Management - Corrosion Monitoring-Cosasco · ppliction ote ecemer Corrosion Management Cossco slescosscocom Controlling Corrosion Upsets in Phosgene Production with Microcor®

Corrosion Management

Cosasco ● www.cosasco.com ● [email protected]

Application NoteDecember 2016

Summary

Corrosion monitoring in the above type of plant is an excellent example of corrosion monitoring for upset conditions, caused here primarily by internal process leaks.

The Microcor ER system can provide fast effective detection not accomplished as easily or as quickly by any other method, thereby preventing expensive and dangerous plant damage.

Read more about Microcor Online Wireless/Wired technologies and corrosion monitoring systems.

Microcor Wireless Corrosion Monitoring System

Microcor Wired Online System