Application
LTTD has proven very effective in reducing concentrations of petroleum products including gasoline, jet fuels, kerosene, diesel fuel, heating oils, and lubricating oils. LTTD is applicable to constituents that are volatile at temperatures up to 1,200 °F. Most desorbers operate at temperatures between 300 °F to 1,000 °F. Desorbers constructed of special alloys can operate at temperatures up to 1,200 °F. More volatile products (e.g. gasoline) can be desorbed at the lower operating range, while semivolatile products (e.g. kerosene, diesel fuel) generally need temperatures over 700 °F, and relatively nonvolatile products (e.g., heating oil, lubricating oils) need even higher temperatures. Essentially all soil types are amenable for treatment by LTTD systems. However, different soils may require varying degrees and types of pretreatment. For example, coarse-grained soils (e.g. gravel and cobbles) may require crushing; fine-grained soils that are excessively cohesive (e.g. clay) may require shredding.
State and local regulations specify that petroleum-contaminated soils must be pilot tested, by some soil from the site being processed through the LTTD system (a "test burn"). The results of preliminary testing of soil samples should identify the relevant constituent properties, and examination of the machine's performance records should indicate how effective the system will be in treating the soil. However, it should be noted that the proven effectiveness of a particular system for a specific site or waste does not ensure that it will be effective at all sites or that the treatment efficiencies achieved will be acceptable at other sites. If a test burn is conducted, it is important to ensure that the soil tested is representative of average conditions and that enough samples are analyzed before and after treatment to confidently determine whether LTTD will be effective.
Operation of LTTD units requires various permits and demonstration of compliance with permit requirements. Monitoring requirements for LTTD systems are by their nature different from monitoring required at a UST site. Monitoring of LTTD system waste streams (e.g. concentrations of particulates, volatiles, and carbon monoxide in stack gas) are required by the agency or agencies issuing the permits for operation of the facility. The LTTD facility owner/operator is responsible for complying with limits specified by the permits and for other LTTD system operating parameters (e.g. desorber temperature, soil feed rate, afterburner temperature).
The decision as to whether or not LTTD is a practical remedial alternative depends upon site-specific characteristics (e.g. the location and volume of contaminated soils, site layout). Practicability is also determined by regulatory, logistical, and economic considerations. The economics of LTTD as a remedial option are highly site-specific. Economic factors include:-
- Site usage (because excavation and onsite soil treatment at a retail site (e.g. gasoline station, convenience store) will most likely prevent the business from operating for a longish time).
- The cost of LTTD per unit volume of soil relative to other remedial options.
- The location of the nearest applicable LTTD system (because transportation costs are a function of distance).
Read more about this topic: Low-temperature Thermal Desorption
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