November Process Puzzler: Consider options for automation

Readers suggest ways to automate an HCl absorber in this month's Process Puzzler in Chemical Processing.

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Question from September's Chemical Processing

We operate an acid regeneration plant (ARP) for a steel mill. In the process, FeCl2 solution is oxidized to Fe2O3 and HCl in a spray roaster; the HCl is recycled to the mill and the oxide is agglomerated and pelletized for feeding back to the mill (Figure 1). Currently, operators do laboratory tests to monitor the quality of HCl (target: 18.5%). The absorber hits an azeotrope at 20.4% at which time the scrubbers become absorbers and we will be fined for an acid emission. Someone suggests monitoring the concentration of the acid in the absorber. e.g., by inferring concentration by measuring conductivity or density, or measuring directly by using an automatic titrator. Automating the absorber also is appealing because this loop requires constant attention, especially during start-up and shutdown. What should we do? Keep in mind that ARPs are water-restricted.

Figure 4. The current PFD of HCl absorption process.
Figure 1. The current PFD of HCl absorption process.

 

Can you support the titrator?

Given the choices named, I would go with the automatic titrator. Density cannot be easily correlated with a Coriolis meter because it depends on temperature and concentration. We found that the best you can do is about ±1% with a Coriolis meter and this just isn’t good enough for contracts with steel companies. They need ±0.5% concentration or better.

A few years ago, I looked at program requirements for using conductivity. The trouble is that the control loop would require constant attention, the set-up would be difficult and the curve relating conductivity to concentration is parabolic. The peak is near 20.4%, the azeotrope. I considered programming that would track the concentration but it became too complicated. So, the least troublesome choice would be the automatic titrator.

The newer models of titrators run about $40,000 installed and do self-diagnostics. They have configuration that permits the frequency of the testing to be run out if the process is stable. You can expect a few problems if you try to duplicate operator testing.

The standard isn’t absolutely stable. We used trietholamine (TEA) as a standard. TEA was chosen because it burns up in the roaster. After sitting around for a few weeks, the potency drops. The result: operators must still do the test ever day or so. If you go with caustic, the standard should be more stable but it can’t be dumped into the pickle liquor sumps, like the TEA, because sodium will contaminate the iron oxide produced in the roaster. The waste from a caustic test must go to the mill wastewater treatment, which is usually restricted for a process handling wastewater.

Another problem is the specific gravity. You could use the daily test to verify the density with a Baume bulb gauge or by weighing on a digital scale. The best approach might be a curve plot of HCl concentration; the titrator could be configured to report the second calculation. One of our engineers tested a curve and it worked well.

By far, the worst difficulty will be reliability. I am a fan of good technology. Used in the right environment it’s wonderful — but a lot of plants don’t spend enough on plant instrument maintenance to support this equipment. Complicated instrumentation becomes more of a liability than a help in the end. I remember — not so long ago — trying to resolve instrument problems overseas. Imagine trying to explain nodes, networks and redundant data paths to them. A 4-20 mA loop is easier to explain and fix — plus it affects only one instrument (unless the wires are shorted in which case it could be a whole card!). It’s often just as bad in the states.

A race car serviced by “shade tree mechanics” isn’t even going to finish let alone win. This philosophy is what concerns me with the automation of the absorber system.

John Brockwell, consulting instrument engineer,
APT technical services, Coraopolis , Pa.

We tried conductivity — not recommended

One of my primary functions is to test the chemistries in these various washers, and to recommend cleaning product additions or tank changes where applicable. To minimize the amount of time taken each day to titrating each tank, it was once proposed that we put several of these tanks on recirculating loops with conductivity meters. The idea was that the conductivities of the various solutions would, once calibrated, give us a daily tank concentration reading for each tank. We believed that this would save time testing tanks. However, this idea was quickly abandoned because of its complexity. Conductivity can be influenced by three solution characteristics, namely: temperature, pH, and dissolved solids concentration. With three potential contributors to conductivity, it becomes difficult to pin down exactly which one is fluctuating at any one time, even with other instruments.

Since the accurate control of the operation of your scrubbers is so critical, I would recommend auto-sampling and/or auto-titration as your preferred test method for measuring the HCl concentration in this stream. It may be a bit more expensive, but it’s also more reliable for testing streams at extreme pH, such as the HCl stream to which you refer.

David Todd site manager,
Cummins Diesel ReCon, Memphis, Tenn.

Automation can also boost morale

For efficient and economic operation of the ARP, control of the acid concentration is necessary. Thus, I would recommend that the possible control technology choices that you have outlined, and others that are available on the market should be compared and one should select the best operational and economic option. Savings during start up and shutdown operation along with need for constant attention will justify the expense. In addition, inclusion of an automatic control scheme would be a morale booster for the operational people. This has benefits that are difficult to dollarize in the justification.

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