| This technology is in the Superfund Innovative Technology Evaluation (SITE) Program. | ||
| This technology is being tested, or has been tested, in EPA SITE Emerging Technology Program. | ||
| This technology is being tested, or has been tested, in EPA SITE Demonstration Program. |
| NUCON
International, Inc. has developed and commercialized an innovative off gas
treatment system using a propriatary combination of hot nitrogen stripping
of adsorbent beds and a reverse Brayton Cycle turbo expansion system to
cool and condense the recovered liquid contaminants. The raw off-gas is processed through carbon beds to remove and concentrate the extracted solvents. These solvents are then stripped and condensed to liquid to minimize the volume of waste disposed. Nitrogen regeneration of carbon adsorption concentration beds eliminates problems of increased volume of the recovered contaminants compared to steam regeneration. This unique process also eliminates the creation of secondary wastewater. The registered trade name of this system is "BRAYSORB". |
| The
NUCON BRAYSORB Solvent Recovery System (SRS) is a new application of well
understood and proven technologies. The engineering and components that
make up a BRAYSORB SRS are all highly reliable and do not require
operation outside industrially accepted practice. The combination and
application is the novel innovation that provides significant advantages.
With only two active components that are simple rotating machines (a
blower and turbo expander/compressor) long term reliability is
exceptional. Energy efficiency is very high based on the use of efficient components and engineered recovery. Over 60 percent of the energy given up by the process gas flow when cooled by passing through the turbo expander is recovered in the turbo compressor. The gas out of the expander is used to precool the inlet gas after the solvents have been passively phase separated. No water is added to the recovered solvents and no secondary waste is created. |
| The
BRAYSORB SRS is efficient only for solvents that are reasonably well
adsorbed on activated carbon and that can be stripped at temperatures
lower than about 350.5 degrees Fahrenheit. The lower the boiling point of the recovered solvents the more advantageous the BRAYSORB SRS is compared to standard mechanical refrigeration systems. |
| The
NUCON BRAYSORB SRS has been successfully demonstrated for soil remediation
off-gas treatment at the DOE Savannah River site. This was done with a
trailer mounted mobile system that has demonstrated the process at a
variety of sites and applications in the U. S. and Canada. Large flow permanently installed BRAYSORB SRS have been in highly efficient operation at production factilities for over five years. There are currently two mobile systems and seven large scale fixed systems in successful operation. |
| Actual | Potential | |
|---|---|---|
| Off-gas generated from a primary innovative treatment technology |
| Actual | Potential | |
|---|---|---|
| Halogenated volatiles | ||
| Nonhalogenated volatiles | ||
| Solvents |
| Actual | Potential | |
|---|---|---|
| Chlor-alkali Manufacturing | ||
| Dry Cleaners | ||
| Gasoline Service Station/Petroleum Storage Facility | ||
| Herbicide Manufacturing/Use | ||
| Machine Shops | ||
| Municipal Landfills | ||
| Paint/Ink Formulation/Use | ||
| Pesticide Manufacturing/Use/Storage | ||
| Petroleum Refining and Reuse | ||
| Other Organic Chemical Manufacturing/Use | ||
| Other Inorganic Chemical Manufacturing/Use | ||
| Semiconductor Manufacturing | ||
| Wood Preserving |
| Number of Full-Scale Systems: | |||
| Number planned/in design: | 1 | Not Provided | |
| MAJOR
UNIT PROCESSES PREPROCESSING -- VOC laden off-gas is generated by some process upstream of the NUCON system. -- Particulate filtration is performed if required. PROCESSING -- VOC laden off-gas is passed through carbon adsorbent beds which remove the VOCs and clean air is discharged to the atmosphere. -- When a carbon adsorption bed has reached its VOC capacity it is taken off-line and regenerated. -- The first step in regeneration is to purge the oxygen from the carbon adsorption bed and system with nitrogen. -- When the oxygen has been reduced to an acceptable level a closed loop flow of hot nitrogen strips the VOCs from the adsorbent. -- The VOCs in the nitrogen are condensed by cooling through a turbo expander and gas to gas heat exchanger for energy efficiency. -- A major part of the energy given up by the gas in turbo expansion is recovered by the compressor side of the turbo unit. The gas to gas heat exchanger also conserves system energy. -- The VOC free nitrogen is heated by the turbo compressor and then the motor driven compressor which is the prime mover of the system. -- The hot clean nitrogen then returns to strip the adsorbent beds until they have been regenerated. POST PROCESSING -- Recovered VOCs are disposed of as water-free liquids. |
| Rank | Factor | |
| 1 | Initial concentration of contaminant | |
| 1 | Target concentration of contaminant | |
| 2 | Quantity of waste | |
| 3 | Labor rates | |
| 3 | Utility/fuel rates | |
| 4 | Site preparation |
| Number of Pilot-Scale Systems | |||
| Number planned/in design | 1 | ||
| Number constructed | 1 | ||
| The mobile pilot plant is a complete BRAYSORB SRS and operates the same as a full-size system described in the full-scale section. |
| Two bench scale systems are in use at NUCON. One glassware 2 cfm and one stainless 10 cfm. These duplicate the full-scale BRAYSORB and BRAYCYCLE Solvent Recovery Systems so all relevant parameters can be determined on a bench scale. |