A Guide to Key Facilities and Sites
at the Portsmouth Gaseous Diffusion Plant
Mary Byrd Davis
Uranium Enrichment Project*
11/04/2000
The following guide, based on US Department of Energy documents,
briefly presents a selection of facilities and sites at the Portsmouth
Gaseous Diffusion Plant. Highlights of the waste streams at certain
facilities are included, but we do not give a complete list of wastes
for any of the locations.
THE CASCADE
1) X-333 Process Building
Carries out the initial phase of the enrichment process. It is
equipped with 80 cells, each of which has 8 isotopic stages, for a total
of 640 stages. All cells contain the largest-size equipment in the
system (designated X-33 or 000). As in the other two process buildings,
the enrichment stages are on the second floor, and the control rooms and
other auxiliary systems and equipment on the ground floor. The two
floors provide a total of 65 acres of floor space.
A Low Assay Withdrawal Station (LAW) is located in the west-central
section of the building. Installed during a cascade upgrading process,
it provides a second station for the removal of reactor-grade material.
(The original low-assay withdrawal station was the Extended Range
Product Station in X-326.) LAW can also withdraw tails.
2) X-330 Process Building
Carries out the intermediate stages of the enrichment process. Thus
it handles UF6 uranium hexafluoride with higher and with lower assays
than X-333. It is equipped with 1100 stages. Five hundred stages (50
cells) are equipped with X-31- or 00-size equipment, and six hundred
stages (60 cells) with X-29- or 0-size equipment. Two floors provide a
total of 55 acres of floor space.
A tails withdrawal station, located in the northeast corner of the
building, was part of the original plant design. It has been modified to
enable it to withdraw product as well as tails.
3) X-326 Process Building
The Portsmouth cascade is capable of enriching uranium to 97% uranium
235. X-326 carried out the final and highest stages of the enrichment
process. Thus it has the smallest process equipment. The building is
equipped with 2340 stages, 720 stages (60 cells) with X-27-size
equipment and 1620 stages, including purge stages, with X-25-size
equipment. The building’s two floors have a total of 58 acres of floor
space.
A withdrawal station known as the X-326 product withdrawal station is
located on the ground floor in the southwest corner of the building. It
was designed for withdrawal of HEU and, like the Extended Range Product
Station, was part of the original plant design.
The Extended Range Product Station (ERP) is located in the northeast
corner of the building. This station was considered safe for all assays
but is usually used for the withdrawal of low-assay UF6.
Purge facilities are located in the south end of the building. It is
necessary to reduce the concentration of light contaminants in the UF6
stream before the upflow enters the small X-25 equipment, which has an
interstage flow that would be too small to handle them. Therefore two
purge cascades are used, each originally composed of five cells. The
side purge, is on the east side of the south end of the building; the
top purge, beside it, on the west side. Under normal operating
conditions, the side purge removed 90% of the light contaminants
present. The top purge removed the remaining 10% and any in leakage into
the purge equipment. Essentially all of the upflow of Freon coolant was
removed at the top purge [DOE 77].
The X-326 L Cage stores "specific levels of radioactively
contaminated waste" under special security requirements [DOE 00a].
Recent history of the Cascade
Production of HEU came to an end in 1991, and 1680 stages were
retired in place. They were cleaned of large deposits and mothballed
between FY 1993 and FY 1998 A total of 240 X-27-size isotopic stages and
180 X-25-size purge cascade stages remain in operation in 2000. They are
used for product withdrawal and side feeding.
From early 1997 to mid-1998, the active stages in X-326 were also
used to downblend 14 MTU of HEU stored at the plant. The downblending
took place as the result of a memorandum of understanding between DOE
and USEC signed in 1994 and was part of "a program to reduce PORTS
inventory of HEU." The HEU-UF6 in storage was refed/down-blended;
and other uranium bearing materials of greater than 20% assay were
shipped off site [BJ 00].
December 9, 1998, a fire largely destroyed one cell and damaged two
other cells in the side purge cascade in X-326. USEC hypothesize that
the fire resulted when an aluminum component of the process equipment
became so hot that it initiated an aluminum/uranium hexafluoride
reaction, which is highly exothermic. USEC decided to repair only the
two less damaged cells.
Feed material for the Cascade
Through FY 1997, 320,817 metric tons of uranium (MTU)
in the form of UF6 were fed to the Portsmouth cascade [BJ 00]. The
major sources of feed material have been the Paducah and K-25 enrichment
plants, which sent uranium hexafluoride (UF6) enriched to a low level to
Portsmouth for further enrichment and also sent to Portsmouth UF6 that
they had produced in their feed production plants but not themselves
enriched. Portsmouth’s X-344 Feed Manufacturing Plant and X-705E Oxide
Conversion Facility produced UF6 feed. Portsmouth also received and
still receives UF6 directly from commercial sources.
Of the 320,187 MTU of UF6 fed to the Portsmouth cascade, 1098.3 MTU
contained reprocessed uranium (reactor tails), according to a study
conducted for DOE on behalf of Bechtel Jacobs [BJ 00]. The sources
included Paducah, Oak Ridge, the Division of International Affairs,
Babcock and Wilcox, the US Atomic Energy Commission Office of Safeguards
and Materials Management, France, and Portsmouth’s own Oxide
Conversion Facility.
The first batch of reprocessed uranium was fed to the cascade during
plant startup--527 MTU that had been converted into UF6 at Oak Ridge and
Paducah from reactor tails entered the cascade between May and September
1955. The last batch, 1.4 MTU, entered in FY 1997-FY 1998.
This last batch was part of the 14 MTU of HEU downblended in X-126 as
the result of the 1994 arrangement between DOE and USEC. Between FY 1968
and FY 1978, small amounts of various assays of reprocessed uranium had
arrived at Portsmouth as part of a government scrap return program. They
came as UF6 or were converted to UF6 at Portsmouth. The 1.4 MTU
downblended in 1997-1998 had come from France (1.1 tons at 56-82%
uranium 235) and NUMEC (0.33 tons at 80% uranium 235) in the seventies [BJ
00].
Air emissions from the cascade
In normal operations the cascade releases a variety of contaminants
to the air, prominent among which are uranium, fluorine/fluorides, and
Freon coolant. A 1987 DOE report lists the following contaminants as
released through the top and side purge cascades in X-326: uranium,
technetium, hydrogen fluoride, fluorine, chlorine, sulfur dioxide,
SO2F2, Freon 114, ClF3, and CF4. Uranium and technetium are named as the
releases from the cold recovery and wet air evacuation systems in X-330
and X-333 [DOE 87].
The exact quantities of uranium and fluorine released from the
cascade over the years will never be known, because of the lack of air
sampling in the early years. Furthermore, the design of the Portsmouth
plant facilitates accidental or intentional venting through unauthorized
and/or unmonitored outlets. "The vast piping and valving
flexibility associated with the cascade buildings offers many
configuration possibilities, including relatively simple means of
rerouting both uranium and fluorine release paths to alternative
locations, such as those that may not be monitored" [DOE 00a].
Fluorine has been a major problem. "Due to Plant design
characteristics, fluorine and fluoride compounds were used in
significant quantities and were required to be vented directly as waste
gases." An estimated 20 to 30 tons of fluorides are released
annually at the plant as a result of routine operations [DOE 00a].
Freon 114, a gas that contributes to the destruction of the ozone
layer, escapes from pipe joints, sight glasses, condensers, coolers, and
valves. USEC has reported in filings with the Securities and Exchange
Commission that Paducah and Portsmouth together lose approximately
750,000 lbs a year. As of 1993, X-333 alone vented approximately 112,390
lbs/yr of Freon to the atmosphere. (In 1993, X-330 contained 1,500,000
lbs of the chemical) [DOE 93].
As for the transuranics and fission products, Bechtel Jacobs
estimates that 0.3 g of plutonium were received at Portsmouth of which
0.003 g entered the process equipment; that 140 g of neptunium were
received of which 46 g entered the process equipment, and that 60 to 90
kg of technetium 99 "were processed." [BJ 00] The report
hypothesizes that any plutonium would have lodged near the feed point;
and that neptunium would have lodged on barrier and unplated surfaces
near the feed point and remained there until equipment change-out.
Technetium 99, on the other hand, was sorbed on metallic surfaces in
the cascade, but, once the entire cascade above the feed point reached
equilibrium, would migrate to the top of the cascade. Operators
installed magnesium fluoride (MgF2) sidestream traps in four cells in
X-126 [BJ 00] and also used portable MgF2 traps to try to absorb
"bubbles" of technetium that advanced through the plant, but
were only partially successful [DOE 87].
Technetium left the cascade through venting to the atmosphere, in the
product stream, and through change-out of equipment. Nevertheless, the
cascade is to this day contaminated with technetium. During the 1998
fire in X-276, "The chemical traps on the process vents became
saturated and technetium was emitted to the atmosphere." A Lockheed
Martin memo of January 6, 1999, states that an estimated 16.6 pounds of
UF6 were released at that time.
Solid wastes from the cascade
Alumina and sodium fluoride (NaF) traps used to prevent UF6 from
escaping into the atmosphere are a major form of solid waste. The sodium
fluoride pellets and alumina were leached in X-705 to recover the
uranium that they contained, if the amount of uranium was thought to
make recovery worthwhile from an economic standpoint. The
depleted/leached traps were buried in the X-749 Contaminated Materials
Disposal Facility [DOE 77].
The quantities of trapping material were not negligible. As of 1993,
the X-330 cold recovery system generated approximately 1000 lbs of spent
uranium-contaminated NaF and 1200 lbs of alumina per year [DOE 93]. As
of 1977, an estimated 700 lbs. of contaminated alumina was removed each
year from the side and top purge traps in X-326. At that time
approximately 75% of the highly enriched UF6 was recovered for return to
the cascade before burial of the residue [DOE 77].
The MgF2 traps presented and still present a major problem, because
technetium 99 has a half life of more than two hundred thousand years.
Some leaching may have been carried out in X-705. A quantity of MgF2
remains on site, but the stream has not been quantified, we are told [BJ
00].
Very large gaskets in the process building ventilation systems were
treated with PCBs. As a result the gaskets dripped oil that "signficantly
exceed[ed]" the regulatory limit for PcBs of 50 ppm. [DOE 00a] The
gaskets also contained uranium. The absorbent material used for cleaning
the drips was mixed with floor sweepings and sent to the landfills.
The depleted UF6 that is a byproduct of enrichment is often
considered to be a waste, although it usually still contains sufficient
uranium 235 to make its enrichment financially profitable under certain
circumstances. DOE stores approximately 161,500 tons of depleted UF6 at
Portsmouth’s X-745 yards. DOE plans to convert the UF6 to a stable
solid.
AUXILIARY BUILDINGS
4) X-300 Central Control Building (1954-present)
Coordinates cascade operations, which are controlled primarily in the
three process buildings. Responsible for the initial response to plant
emergencies. The dome-shaped building is east of the X-326 Process
Building. It is constructed of reinforced concrete and designed to
resist blasts and shocks [DOE 77]
5) X-342 Feed Vaporization and Fluorine Generation Facility (1954-present)
The facility is used to feed, vaporize, and sample UF6 (uranium
hexafluoride) and to generate and purify fluorine. Originally X-342 fed
the cascade [BJ 00]. The primary current role of X-342 is generating
fluorine, which it does for the entire plant Hydrogen fluoride (HF) is
converted to fluorine by an electrolytic process. X-342 now serves as a
backup to X-343 and X-344 for the feed, vaporization, and sampling of
UF6.
Waste products from fluorine generation and purification were sodium
fluoride, lithium fluoride, and potassium fluoride, in addition to
hydrogen fluoride and fluroine [DOE 93 ].
6) X-343 Feed Vaporization and Sampling Facility (1983-present)
Vaporizes UF6 for feeding to the cascade. The UF6 is received in
solid form. X-343 is located approximately 200 ft to the east of X-333
and is connected to the X-333 feed header system. The facility can also
sample UF6.
7) X-344 Feed Manufacturing Plant (1958-1962)
(The Feed Plant was located for the most part in what are now the
X-342A Feed Vaporization and Fluorine Generation Building and the X-344A
UF6 Sampling Facility [BJ 00]. Other buildings with the name X-344
followed by the letters B, C, E, F, or G performed various auxiliary
activities.)
X-344 converted uranium tetrafluoride (UF4) to uranium hexafluoride
(UF6).
The plant included four fluorination towers, two cleanup reactor
towers for scavenging excess fluorine gas, compressors and cold traps to
collect the UF6, and cylinder fill stations.
UF4 in powdered form and fluorine gas were fed into the tops of the
towers. The resulting UF6 passed through filters and then into cold
traps, where the UF6 solidified. The traps were connected to empty
cylinders and heated so that the gas flowed into the cylinders. The
cylinders were then moved to the cascades into which the UF6 was
fed.
Feed
The UF4 fed into the plant came from Mallinckrodt Chemical Works (MCW)
and National Lead of Ohio (NLO) now known as the Fernald Feed Materials
Production Center. According to plant records, none of the UF4 contained
reprocessed uranium [BJ 00].
However, from August 1958 until October 1961 purge gas from the
cascades was processed in the Feed Manufacturing Plant’s cleanup
reactor towers to recover excess fluorine. Therefore the plant may have
received technetium from the cascades. In fact, a sharp increase in the
plugging of filters at the plant after the introduction of the gas from
the cascades would seem to indicate that technetium had indeed come with
that gas. Furthermore, the plant could have received some transuranics
along with the uranium recovered in X-705 from plant effluents and
returned to the plant [DOE 00].
Production
UF4 was fed at an average rate of 9.5 MTU per day. The facility
produced a total of 11,890 MTU of UF6 [BJ 00].
Off streams
Ash fell into receptacles that were taken to a storage area.
Radiation near the ash receivers was high, as uranium daughter products
tended to concentrate in them [DOE 00a]. The radioactivity in the ashes
was allowed to decay for two to six months. Then the ashes were blended
with the incoming UF4 and refluorinated in the towers. When the
installation closed in 1962, the ashes that remained were sent to
Paducah for uranium recovery.
Liquids from decontamination of filters and from maintenance were
sent to X-705 for recovery of the uranium. The recovered uranium was
returned to X-344, blended with the incoming UF4, and fed into the
fluorination towers.
In the plant, leaks and spills of UF4 and ash "presented
continuing problems with surface and airborne contamination." The
Feed Plant was a major contributor to uranium releases, as it lost an
average of 407 kg of uranium (0.22 Ci) per year to the atmosphere from
1959 to 1962. Releases from Portsmouth as a whole dropped sharply in
1963 after the shutdown of the plant [DOE 00a].
Waste acid from a water scrubbing system for gaseous effluents was
neutralized with lime and then released to the sewer.
8) X-344A UF6 Sampling Facility
The building originally housed the process equipment, offices, and
maintenance areas for the X-344 Feed Manufacturing Plant (see above).
The building was abandoned in 1962 after feed production ceased. In the
early 1970s work on converting the building began, but during
construction a fire caused the explosion of a propane tank. The
explosion "destroyed much of the immediate area" and caused a
portion of the second floor to cave in. Work was resumed after two years
and completed in 1975. The building housed the High Assay Sampling Area
(HASA) for a time. The former HASA is now a storage area.
X-344A currently handles the sampling and the transfer of UF6 from
one cylinder to another. Toll product is withdrawn from the cascade into
10-ton DOE cylinders and then transferred here to 2.5 ton commercial
shipping cylinders.
9) X-345 Special Nuclear Materials Storage Building (around
1978-present)
North and South vaults store or stored highly enriched uranium. The
central area houses a high-assay sampling area (HASA) and a small
laboratory. The area around the HASA is known to be contaminated.
"The available documentation designates the entire building as
having fixed radiological contamination," although the custodian
told DOE that the contamination is localized [DOE 93]. DOE describes the
sampling facility as a source of fluoride and uranium emissions [DOE
00a]
10) X-626-1 Recirculating Cooling Water Pump House and X-626-3
Cooling Tower
X-626-1 and X-626-3 circulate and recirculate water that is used to
remove the heat of compression from the process gas, along with waste
heat from a few auxiliary processes, and to dissipate this energy to the
environment. They, like systems connected with the X-330 and X-333
process buildings function as an independent unit for the most part, but
they belong to an overall plant-wide recirculating cooling water system
(RCW). (See below for the X-330 and X-333 facilities
Each process building’s cooling system consists of a primary loop,
which comes into contact with the hot UF6, and a secondary loop, which
receives the heat through a heat exchanger and carries it to the cooling
towers. In the cooling towers, the heated water in the secondary loop
comes into contact with cool atmospheric air, which absorbs the heat.
The heated air is discharged at the top of the tower and the cooling
water falls through the tower, is collected in a basin below the tower
and then recirculated.
To limit the amount of concentration of solids that will occur in the
recirculating water, a quantity of water called blowdown is removed from
the system continuously to remove dissolved solids. Blowdown water is
routed from the X-626 system through the X-630 system to the X-633
system and thence to the X-616 treatment facility [DOE 77].
Wastes
The recirculating water system discharges water vapor and some
particulate matter, which is a product of the drift emissions. Solids in
cooling tower drift as of 1977 were chromium, zinc, copper, iron,
chloride, sulfate, silica, and sodium pentachlorophenate [DOE 77].
Sodium pentachlorophenate is a fungicide that, before 1982, was used to
treat the wood of the cooling tower. After 1982 cupric arsenate was
applied to the wood. An unknown quantity of the fungicides may leach
into the cooling water, a 1993 report states Freon 114 (a coolant) and
freon 113 (a solvent) had been detected in cooling water prior to 1993
and was reported as a potential contaminant. The Freon compounds
apparently entered from the process building coolant systems at a
minimum rate of 60,000 pounds per year [DOE 93].
Until June 1989 the plant added to the cooling water a hexavalent
chromium-based composition to inhibit corrosion. This material was
replaced at that time with a phosphate-based formula, but chromium
lingered for a period in the recirculating water. "In 1991 it was
reported, using best engineering judgment, that 860 lbs of chromium and
140,000 lbs of chlorine (in the form of HOCl) were released into the air
via stacks [DOE 93]. (According to DOE’s Investigative Report, the RCW
treatment system was switched to a phosphate-based inhibitor in 1991,
not 1989 [DOE 00b]).
In 1991, 710 lbs of chromium were estimated to have been released
into the Scioto River [DOE 93]
11) X-630-1 Recirculating Cooling Water Pump House, X-630-2A and
X-630-2B Cooling Towers, and X-630-3 Acid Handling Station
(see X-626 above on the cooling water system)
12) X-633-1 Recirculating Cooling water Pump House, X-633-2A,
X-633-2B, and X-633-2D Cooling Towers
(see X-626 above on the cooling water system)
13) X-700 Maintenance Building (1954-)
The building is used for equipment maintenance support for
non-radioactive or low-level radioactively contaminated equipment from
the diffusion cascade. It houses Chemical Cleaning and Operations, the
Converter/Weld Shop, and the Radiation Calibration Lab. The Chemical
Cleaning and Operations has been modified as needs have changed. It
included a stabilization area or furnace stand, where workers pretreated
converters with heated fluorine gas before installing them in the
cascade. Fluorine gas was piped into the building for this purpose.
Chemical Cleaning also had two vapor degreasers, both of which began
operation in 1955. One was shut down around 1975 and removed in the
early 1980s. The other was shut down in 1988, but in 1993 was still
present [DOE 1993]. Heated TCE was used for degreasing until 1987;
1,1,1,-trichloroethane has been used since [DOE 00b].
Releases
The degreasers generated about 500 to 1000 gallons monthly of air
emissions of evaporated TCE or TCA [1993, 275].
In the stabilization area, the fluorine gas, after use, "was
vented, directly into the air 8 to 10 ft above the ground, along with
heat emissions" [1993, 275].
TCE that entered floor drains went, via a sump, to the X-701C pit,
from which it was sent to the X-701B holding pond. X-700 was the major
source of TCE in X-701B and in the entire east drainage ditch area [DOE
70].
14) X-705 Decontamination and Recovery Facility (1954-present)
[DOE 16]
As of 1993 the building housed five operations: process equipment
disassembly and decontamination, small parts cleaning and
decontamination, recovery of uranium from decontamination solutions,
routine chemical analyses, and laundry of company clothing worn by plant
personnel (we describe below only the first two of these five
operations). From 1957-1978 the conversion into uranium hexafluoride of
uranium recovered from the decontamination solutions and of other
uranium materials also took place in the building.
A. Equipment decontamination
Workers disassembled large parts of cascade equipment, vacuumed them
to remove uranium compounds, and treated them in a "decontamination
tunnel, "a series of five spray booths. The first three booths
contained recirculating nitric acid, ammonium carbonate, and rinse water
[DOE 77] or nitric acid, citric acid, or acetic acid solutions [DOE
00a]; the fourth used nonrecirculating rinse water, and the fifth was a
drying chamber.
Workers disassembled and decontaminated compressor seals and other
small parts by hand in the "seal disassembly room." They used
recirculating water, nitric acid, and ammonium carbonate solutions at
four hand tables. The parts, after being treated at the hand tables,
went to a "steam pit" with steam guns and small containers of
nitric acid, alkali, and isopropyl alcohol for removal of the "last
traces" of uranium [DOE 77].
Empty feed/product cylinders were cleaned to decontaminate them and
remove heels (nonvolatile materials that remain in cylinders after the
UF6 that they contain is vaporized by heating). If the UF6 was made from
reprocessed uranium, they contain transuranics, fission products, and
irradiating daughters of uranium 232. In the 1950s and 1960s, cylinders
were hosed down in an open area, where wash water spilled onto the
floor. After November 1970 a closed "cylinder decontamination
facility" was installed. Cylinders were placed in a turning fixture
and connected to piping through which boric acid and sodium carbonate
cleaning solutions and rinse water were recirculated. The cylinders were
then heated in an enclosed drying booth [DOE 00a]
Off streams
Acid solutions from the spray booths and seal disassembly room, and
cleaning and rinse solutions from the cylinder decontamination facility
were sent to the Uranium Recovery Facilities [DOE 00a].
As of 1993 wastewater from the decontamination operations was treated
in X-705 before discharge to the sanitary sewer and then further treated
in the X-6619 Sewage treatment Plant before discharge to the Scioto
River. The treatment systems were designed to dentrify and to remove
heavy metals. However, monitoring at the outfall for X-705 detected in
1991 copper, iron, nickel, and zinc at maximum levels of 499 picog/l,
7890 picog/l, 728 picog/l, and 1040 picog/l respectively.
Also, as of 1993 the building’s sump water contained a high level
of TCE, which may have been coming from groundwater. The sump water was
pumped and trucked to the X-622 Carbon Filtration Facility for treatment
[DOE 93].
B. Uranium Recovery Facilities
Area B of the X-705 building recovered uranium from a variety of
liquid solutions and solid waste materials
Feed material
Ashes and filtrates from UF4 conversion, oxide
conversion, and incinerators, solutions from cylinder washing, other
decontamination solutions, alumina and sodium fluoride pellets from
traps in the oxide conversion facility and the cascade, filters from
ventilation systems, vacuum cleaner particulates, laboratory wastes,
materials from spills, and uranyl nitrate hexahydrate (UNH) from
reprocessing operation(s) abroad. Some magnesium fluoride traps may also
have been leached here [BJ 00]. Materials from the oxide conversion
facility and the UNH from foreign sources were contaminated with
transuranics [DOE 00a].
Processes
The basic facility used a solvent extraction process, which involved
dissolving uranium oxides in nitric acid, removing any insoluble solids,
evaporating the liquid to reduce its volume, separating uranium from
contaminants by solvent extraction pulse columns, drying the uranyl
nitrate solution in a drum dryer, and passing the resulting material
through a calciner and rolling mill to produce dry triuranium octoxide
(U3O8) [DOE 00a].
For UNH, the treatment differed. Crystals of UNH were dissolved in
water. The solution was fed to a rotary calciner, where the water
evaporated and the UNH melted. Denitration took place, and the UNH
became UO3. The UO3 moved down the calciner into a hotter zone, where it
was reduced to U3O8 [DOE 77]. UNH produced by reprocessing in a foreign
country or countries was converted to oxide in the calciner during at
least 1965, 1966, 1975, and 1976 [DOE 00a].
Production
Peak production of U3O8 occurred in FY 1960 with
the processing of 8 MTU, probably as a result of processing
decontamination solutions from the first change-out program in the
cascade. Total production through March 1999 is about 38.2 MTU [BJ 00].
While the Oxide Conversion Facility was in operation, the U3O8 was sent
to it for conversion to UF6 preparatory to enrichment in the cascade.
Waste
Waste from the recovery process is mainly the depleted acid (raffinate)
from the extraction column. Starting in 1975, technjnetium and
transuranic contaminants were identified in liquid process effluents
from X-705. Transuranics stayed with the uranium for the most part, but
technetium 99 entered the raffinate stream. The raffinate stream also
contained uranium daughter products. This stream was "initially
discharged to an onsite ditch that flowed to Little Beaver and Big
Beaver Creeks, and then to the Scioto River." Subsequently the
raffinate was directed to an onsite settling pond, X-701B [DOE 00a].
During 1984, the discharge to X-701B was permanently suspended with the
startup of the heavy metals precipitation process (X-705), technetium 99
ion exchange process (X-705), and biodentrification process (X-700) [BJ
00].
The calciners released nitrogen oxides to the building roof vent. As
of 1977 a total of approximately 5600 pounds of nitrogen oxides were
emitted annually from calciners in the B and F areas of X-705 [DOE 77].
C. Oxide Conversion facility (1957-1978)
(According to a source published in 2005, the Oxide Conversion
Facility was located in the E, F, and H areas of X-705 [BJ 00a]. A
September 1977 EIS on a possible plant expansion, which includes a
diagram of X-705, placed it in Section C. Possibly the sections have
been renamed. According to DOE’s May 2000 investigative report, the
oxide conversion areas were "physically separated" from the
decontamination and recovery areas described above [DOE 00a]).
Process
Oxide conversion used a one-step process to convert oxides of uranium
into uranium hexafluoride by direct fluorination .
The original system was composed of three stirred-bed reactors. In
1959 these reactors were replaced by a four-inch-diameter open flame
tower, with a nominal capacity of 7200 kgU/yr output as UF6. This
system, which involved manual handling of fine uranium oxide powder, was
dismantled and removed. A new system, with more automated processes and
glovebox enclosures and with a nominal capacity of 20,000 kgU/yr output
as UF6, was installed in 1967 in preparation for the processing of
oxides from irradiated fuel. It centered in an improved five-inch flame
tower.
U308 was ground and fed through the top of an air-cooled flame tower
into an elemental fluorine atmosphere, where there was a spontaneous
flame reaction between the oxide and the fluorine, which produced UF6
and oxygen. The UF6 was passed through a sintered metal filter to remove
particulates and then through a MgF2 trap for sorption of certain
impurities [BJ 00]. It was then withdrawn into cold traps where it
solidified. Cold traps were removed and heated to liquify the UF6. The
liquified UF6 was drained into cylinders for feeding to the cascade.
The oxide that did not react during the first pass through the tower
was collected in an ash pot at the bottom of the tower and subsequently
pulverized and refed to the tower. Most of the impurities in the oxide
were filtered from the gas stream in a secondary disengagement section.
The "filter ash," which was less than 1% uranium, was
processed through the Uranium Recovery Facilities [DOE 77].
In theory any plutonium should concentrate in the tower ash and
filter ash, and neptunium in the MgF2. In actuality, the pathways
followed by plutonium and neptunium depended on several variables. As
much as 85% of the neptunium and 57% of the plutonium may have ended up
in UF6 product cylinders. The filter ash would contain the majority of
the remainder of the transuranics [BJ 00].
Feed
The conversion facility received uranium from at least 47 sources [BJ
00]. Raw material was produced in X-705’s Uranium Recovery Facilities
through uranium recovery operations and through conversion of uranyl
nitrate hexahydrate (UNH) from off-site sources. It also came in the
form of oxides directly from commercial processors, and from
"government sources" [DOE 00a]. It is reported that 5.6 MTU of
feed contained transuranics [BJ 00]. According to a memorandum of
September 20, 1978, the facility handled highly enriched uranium, at
least during a July 1978 "test run, utilizing 97% material,"
which resulted in a "number of unexplained high airborne
samples."
Production
The facility produced about 233 MTU of UF6 [BJ 00].
Waste
An unknown quantity of filter ash went through Uranium Recovery to
create U3O8 for a second attempt at conversion to UF6. "The filter
ash that remains on-site is stored in the X-326 "L" Cage.
Some of the magnesium fluoride may have been treated in Uranium
Recovery. An unknown quantity, some of which may have come from the
Oxide Conversion Facility, remains on site.
The sodium fluoride was regenerated through in-place heating, and
also treated in Uranium Recovery to leach out the uranium.
Depleted/leached media was placed in cans, the cans packed in wooden
boxes in which lime filled the spaces, and the boxes buried in the
X-749A landfill [BJ 00].
"Very high airborne concentrations of radioactive material were
prevalent in the oxide conversion facility" and "could have
been vented to the atmosphere through penetrations, ventilation systems,
doors, and windows." According to a 1977 report, an unfiltered
exhaust system vented air through a roof stack [DOE 00a].
Current situation
Operations were ended, because the "facility
could not meet current standards for containment as manifested in high
levels of airborne contamination." Attempts to upgrade or replace
it were terminated in July 1981, when cost estimates proved to be
prohibitively expensive. DOE’s 1993 audit states that "the E
area, which is in the northeast part of the building, is sealed and no
longer used because of contamination from transuranics. This area . . .
is highly radiologically contaminated. According to interview responses,
it is highly probable that over the years incidental releases of the
highly concentrated and toxic chemicals used in this building have
impacted the soil directly under and around the building. Groundwater
may also be affected" [DOE 93]. There are currently "no known
funded plans for Decontamination and Decommissioning" this facility
[BJ 00].
D. X-705 Annex
The annex was created for the disassembly and decontamination of
large pieces of equipment from the cascades that were contaminated with
high levels of technetium. Operations also included regeneration of
alumina traps.
According to the DOE 2000 investigative report, the area had the
"highest average airborne contamination in the X-705 complex."
Air was released "through absolute filters to reduce airborne
emissions to the environment" [DOE 00a].
15) X-710 Technical Services Building (195?-present)
Building X-710 houses laboratories and facilities that provide
technical support and development activity to the plant. Because
development of processes and procedures for the plant has been an
integral part of the facility’s mission for most of its life, "a
myriad of experiments" that involved transuranics and fission
products have been carried out there. They involved "minor/trace
amounts of these elements/isotopes" [BJ 00].
16) X-710B Building
The building, west of Building X-710, was an explosion-proof testing
facility. As of 1977, "dangerous laboratory and pilot-plant-scale
experiments [were] carried out in this building. Occasionally dilute
chlorine trifluoride and fluorine [were] vented to the roof" [DOE
77]
16a) X-720 Maintenance and Stores Building
17) X-744G Bulk Storage Warehouse (now the Uranium Management
Center?)(195?-present)
Initially the building was a pipe fabrication facility, where
operations included degreasing the interior surfaces of pipes with
organic solvents. Later, but still in the early years, it served as the
non-UF6 and small cylinder UF6 storage area. Overflow materials from
X-705 were also stored here. The DOE investigative report stated that
X-744G was "used for several years to store spent chemical trap
materials, miscellaneous dried sludges, and ash from the X-705
incinerator," which included RCRA wastes [DOE 00a].
When, around 1996, the scrap return program was initiated, the
building was designated as the scrap storage warehouse and central
receiving facility. Thus it received oxides, UNH, and small cylinders of
UF6. Non-UF6 containers were opened and sampled. All oxides were stored
in the building until, around 1978 when, with the opening of X-345, HEU
materials went to that facility.
In recent years the building was renovated to store uranium in
quantity. The Draft Environmental Impact Statement on the dispatch of
surplus Hanford site uranium to Portsmouth states "Building 744-G,
the primary receipt facility under consideration, has been upgraded . .
. The facility, termed the Uranium Management Center, is expected to
house a total of approximately 5900 MTU (13,000,000 pounds) of uranium
materials" [DOE 99b].
In August and September 1999 X-744G received shipments of uranium
materials from the Universities of Seattle and Nebraska respectively.
The January 2000 issue of the Portsmouth Environmental Bulletin
describes the shipments as totaling 20 MTU that DOE had previously
loaned to these two universities for purposes of research and education.
However, the September 2000 issue of that publication states that
Portsmouth is receiving about 20 MTU that DOE lent to "various
universities around the country," and DOE announced at a public
meeting January 27, 2000, that Portsmouth had received in 1999 for
storage 2.2 MTU of aluminum-clad metal slugs with uranium enriched to
0.947% from the University of Seattle and 2.5 MTU of aluminum-clad metal
slugs with "normal" uranium from the University of Nebraska.
In 2000, Fernald is in the process of shipping 3800 MT of depleted
and natural uraniium to Portsmouth for storage. Shipments should be
complete by late 2001. The uranium is being sent to X744-G "for
interim storage."
In June 2000, DOE issued a Finding of No Significant Impact on plans
to ship to Portsmouth from DOE’s Hanford site, for storage,
approximately 900 MTU composed of uranium metal billets (235 MTU),
low-enriched uranium trioxide powder (approximately 670 MTU), and
uranium dioxide and depleted uranium in various forms (approximately 4
MTU). This uranium is "readily saleable," DOE claims [DOE
00b].
The "Recycled Uranium Mass Balance Report" describes X-744G
as currently "support[ing] the DOE PORTS Uranium Management Center
activities. Quantities of materials containing TRU are being stored here
as part of this program. These materials were received after the March
1999 timeframe" for the report [BJ 00]. Of the materials at X-744G
known to the public, those from the Universities of Seattle and Nebraska
would seem to be the most likely to contain transuranics.
While serving as a storage center, the facility has also in the past
been the center for other activities. A smelter for scrap aluminum,
primarily parts of compressors, was located here from 1961 through 1983.
Material went through a decontamination process before being melted,
but the unit experienced problems with "airborne
contamination." Uranium contamination in the feed tended to stay
with the melted aluminum. Nevertheless, "aluminum ingots were sold
for unrestricted use" as well as used for replacement parts for
cascade equipment [DOE 00a].
X-744G was a source of radionuclide and fluorine releases [DOE 00a],
perhaps in connection with the smelting of aluminum.
18) X-746 UF6 Sampling and Shipping Center
DOE investigators heard from people they interviewed in 1999/2000
that "a massive release" occurred in X-746. It is used in 2000
for personnel and administrative functions [DOE 00a]. The 1993 audit
describes the building as a "Shipping and Receiving Building"
[DOE 93].
19) X-760 Chemical Engineering Building
The building’s mission was pilot-scale development work on new
chemical processes prior to or in aid of plant development. "Early
development projects, including decontamination process experiments,
boiling freon heat exchanger experiments, UF6 heating studies, uranium
oxide pelletizing experiments, freon drying tests, and controlled UF6
releases in a sealed environmental chamber, were conducted in this
facility." Here also was done development work on the "fluorox
process," which appears to have involved a prototype fluorination
tower for the Feed Manufacturing or Oxide Conversion Facility. According
to records X-760 received, from K-25 in 1957, 0.86 MTU of UF4, 0.4 MTU
of UO2, and 3.3 MTU of UO3 classified as recycled uranium. Likely, any
materials converted to UF6 in X-760 were fed to the cascade, and
materials not converted there were converted to UF6 in X-705 when it
began to operate. [BJ 00].
GAS CENTRIFUGE ENRICHMENT PLANT (GCEP)
20) X-3001 Gas Centrifuge Enrichment Plant (GCEP) Process Building
#1
Construction of a gas centrifuge enrichment plant began at Portsmouth
in 1979. It was halted, before the plant was completely built, in 1985.
The GCEP installation consists of numerous facilities, including a
Switch House, Switch Yard, and Centrifuge Training Facility. Only four
are mentioned here.
According to Inside Energy (December 7, 1987), DOE in 1987
sold 1300 unused centrifuges to a Tennessee company, AlChemIE, which was
to use them to enrich non-uranium stable isotopes. X-3001 and X-3002 are
reportedly today basically empty buildings.
DOE announced October 6, 2000, that it will again develop centrifuge
enrichment capability. Initial work will take place at Oak Ridge, but
within a year the focus will shift to Piketon. Existing facilities will
be refurbished to house a demonstration project.
21) X-3002 GCEP Process Building #2
22) X-3346 GCEP Feed and Withdrawal Facility
23) X-7725 GCEP Recycle/Assembly Building (X-7725 storage Unit) (1983-present)
This building was converted into an approved mixed waste storage
facility in 1992. It has five floors with a total of 20 acres of floor
space. A RCRA Part B storage permit was issued by Ohio Environmental
Protection Agency in August 1995. At the present time the facility
stores all plant mixed and hazardous waste, except that stored for
security reasons in X-326 L Cage. [DOE 00a] It also stores low-level
radioactive waste and Toxic Substances Control Act waste. This building
also provides office space.
STORAGE YARDS
24) X-745 Cylinder Storage Yards
At least eight (A-H) cylinder storage yards exist or have existed at
Portsmouth. All DOE-managed cylinders with depleted uranium hexafluoride
(cylinders containing depleted UF6 produced before DOE leased enrichment
facilities to USEC) are stored in cylinder yards X-745-C (C yard) and
X-745-E (E yard). These yards store a total of 13,388 cylinders. The
cylinders in Yards C and E contain approximately 161,500 tons of
depleted UF6.
As of 1998, another yard, X-745-G, stored 2800 United States
Enrichment Corporation (USEC)-generated cylinders. The X-745-G yard is
just outside the perimeter road that defines what is known as the
Portsmouth Uranium Enrichment complex.
The heels of cylinders that contained reprocessed uranium and were
not subsequently decontaminated/washed would contain transuranics,
fission products, and the daughters of uranium 232 (bismuth 212 and
thallium 208, emitters of hard and intense gamma radiation). It is
possible that some cylinders were emptied and refilled several times
without washing, which would have concentrated the contaminants.
Several small diameter UF6 cylinders containing highly-enriched
reprocessed uranium were received from offsite sources in the seventies.
Most of this HEU was only fed to the cascade around 1997. The cylinders
were then cleaned in X-705 or at Nuclear Fuel Services. The solution
from the cleaning at X-705 is stored, in blended down form, in X-705,
because of operational problems at that facility. What happened to the
cylinders sent to Nuclear Fuel Services and their solutions is not known
[BJ 00].
25) X-747-H Northwest Materials Storage Yard or Scrap Metal Yard (1978-present)
The yard stores over 7 million pounds (32,700 cubic meters) of scrap
materials. It occupies approximately 6.8 acres and, as of 1993, was
surrounded by a chain-link, barbed-wire fence. The stored material
includes large metal cascade scrap that has gone through a
decontamination process in X-705/X-700 [DOE 93]. "The vast majority
of the material is contaminated and has been in storage since the
1970s," DOE said in its recent investigative report. In early 2000,
plans were being made to sort, repackage, and ship a portion of the
scrap metal [DOE 00a].
26) A Hot Yard (1960s through 1979)
Management moved the contents of this apparently unnumbered Hot Yard
to X-747H during the 1979 strike. The Hot Yard was located "south
of X-751 to the X-230-K South Holding Pond, and extend[ed] past the end
of the current X-2207A parking lot [DOE 00a].
27) Small Hot Yard
Southwest of X-326, this yard was used to store semi-precious metals
(copper and brass).
LIQUID WASTE MANAGEMENT AND TREATMENT FACILITIES
28) X-231A Oil Biodegradation Plot (1971-1977)
At Portsmouth waste oils were treated according to a process
developed in Oak Ridge. However, the fertilizing and tilling or disking
that the process required were not adequately implemented.
"Approximately 24,500 gallons of waste oil contaminated with
solvent and radionuclides, 124,300 pounds of oil-soaked fuller’s
earth, 60 gallons of TCE, and 1,000 gallons of chlorinated solvents were
applied at the X-231A oil biodegradation plot." The area was
temporarily capped in 1987 as part of an interim remedial measure [DOE
00a].
29) X-231B Oil Biodegradation Plot (1976-1983 [DOE 99c] or
1981-1977 [DOE 00a])
The site consists of two disposal plots, each surrounded by an
elevated soil berm. It was used for "land application" [Port
99c] of uranium-contaminated waste oil, PCBs, and solvents [DOE 00a]. No
records were kept of the quantity of solvents applied [DOE 00a] After
use ceased, the site was treated "to remove volatile organic
compound contamination present in the soil" [Port 99c]. The site
was temporarily capped in 1987 as part of an interim remedial measure
[DOE 00a].
30) X-611A Lime Sludge Lagoons (1954-1960)
The three Lime Sludge Lagoons collected waste lime
from the X-611A Water Treatment Plant from 1954 to 1960. From 1956 to
1957, chromium-laden lime sludge, from cooling water used in the uranium
enrichment process was disposed of in the lagoons. Chromium had been
used in the cooling water as a rust inhibitor. The sediment has been
left in place but the lagoons covered with a geotextile fabric topped
with soil sown with prairie grasses. The work was completed in 1996.
31) X-616 Liquid Effluent Control Facility (1976- )
The facility was constructed to treat cooling water blowdown in order
to meet the permitting process put into place by the 1970 Clean Water
Act [DOE 68]. It reduced hexavalent chromium to trivalent chromium by
adding sulfur dioxide to the water. The treatment resulted in the
precipitation of chromium hydroxide sludge. Treatment was suspended in
1990 after the chromium-based inhibitor had left the system. X-616 also
treated effluent from the X-700 Chemical Cleaning facility and the X-705
Decontamination Building [DOE 93].
Waste
The chromium hydroxide sludge formed as a result of treating
hexavalent chromium was stored in two surface impoundments to the west
of the facility. Closure of the impoundments began in 1990. At that time
the sludge was removed, treated, and placed in the X-735 landfill [DOE
93]. In 2000, the sludge, more than six million pounds in total, is
being shipped to Envirocare in Utah for disposal, according to the
Portsmouth Environmental Bulletin, Sept. 2000.
Treated water was piped to the Scioto River [DOE 00a]. According to
1991 monitoring data, the maximum concentrations of hexavalent chromium
and total chromium were 20 micrograms/liter and 1560 micrograms/liter
respectively [DOE 93].
32) X-701C Neutralization Pit and Pump Pit (?-1988)
Received contents of the sump that was in the X-700 Chemical Cleaning
Facility, which was contaminated with TCE. The waste then went to the
X-701B holding pond. The pit was closed in 1988 [DOE 00a]
33) X-701B Holding Pond (?-1988)
This unlined pond was "used for the neutralization and settling
of metal-bearing waste water, solvent-contaminated solutions, and acidic
waste water." Most of the waste came from the X-700 Chemical
Cleaning Facility and the X-705 Decontamination Building [DOE 00a]. As a
result of the decontamination of material that had been in contact with
reprocessed uranium, an estimated 1415 grams of technetium were sent in
the raffinate to the holding pond. Furthermore, 0.03 grams of plutonium
and 3.3 grams of neptunium were measured in the X-701B sludge when it
was characterized for low-level waste disposal [BJ 00].
In 1972 facilities to feed slaked lime and photoelectrolyte to
neutralize the low pH and promote the precipitation of uranium along
with transuranics and technetium, were added. Once or twice a year, the
pond was dredged or sludge pumped to containment ponds next to the
settling pond.
During 1984 the discharge of raffinate to X-701B was permanently
suspended due to the startup of treatment processes in X-705 and X-700.
X-701B and the two containment ponds have been dredged and their
contents and the first foot of soil beneath them packaged. Portsmouth
has shipped the sludge to the Envirocare disposal facility in Utah.
The pond was a major effluent source to Little Beaver Creek [DOE
00a].
SOLID WASTE MANAGEMENT, TREATMENT, AND DISPOSAL FACILITIES
34) X-749B Peter Kiewit Landfill (1954-1968)
During construction of the plant, an area south of the main buildings
was used for the disposal of construction waste. Named after the
construction contractor, the area became the site’s landfill after
initial construction was completed. [DOE 00a]
As an interim remedial measure to take care of surface seeps,
adjacent Big Run Creek was rerouted, and a seep collection/treatment
system installed in the original creek bed. A cap was installed on the
landfill in 1998 [DOE 99c].
35) X-734 Old Sanitary Landfill (1968-1991)
The 16.2-acre X-734 landfill was opened for the disposal of
construction spoils, after it became clear that construction would
continue at the site. Plastic containers, waste drums, and chemical
product containers were buried there in addition to construction waste,
despite rules to the contrary. After a 1985 user questionnaire revealed
the contents, the site was closed and waste sent to X-735 [DOE p. 61]. The
landfill has been capped with compacted soil and a vegetative layer. The
capping of the last portion was completed in July 2000.
36) X-735 Sanitary Landfill (1981-1997)
The southern portion of the landfill contains asbestos, floor
sweepings,, sanitary waste, and sewage plant coarse screenings. The
northern portion contains these materials and rags used to remove
solvents in the X-720 paint shop. Because of the rags, the northern part
of the landfill had to be closed according to RCRA hazardous waste
facility closure regulations. The southern part was closed according to
State of Ohio solid waste regulations [DOE 00a]. Closure was completed
in 1998 [DOE 99c].
37) X-749 Contaminated Materials Disposal Facility (northern
portion 1955-1990; southern 1986-1990)
The landfill received "alumina-trap residue, sodium fluoride,
incinerator ash with trace quantities of neptunium and plutonium,"
among other materials. [DOE 00a] Disposal volumes throughout the 60s and
early 70s were in the hundreds of cubic feet a year. A 1976 report on
waste disposal, stated that "much of the chemical trap material
contained technetium-99, which is highly water soluble." Following
the report, the chemical trap material was placed in sealed packages
before disposal, but it had been buried without packaging for almost
twenty years.
Between August 1984 and June 1985, approximately 85,000 pounds of
metal hydroxide sludge from the X-705 raffinate was buried at this
facility, although the sludge could leach cadmium. The State of Ohio EPA
directed that the landfill be closed, because of the inappropriate
burial of such RCRA waste. It closed in 1990 [DOE 00a ]. Closure
included the installation of a multimedia cap, a slurry wall, and
subsurface groundwater drains [Port 99c].
38) X-749A Classified Materials Disposal Facility
(1953-1988 )
This site was operated for the disposal of wastes classified under
the Atomic Energy Act and was intended to meet the needs of Portsmouth
"and other DOE and non-DOE facilities" [DOE 00s]. All
materials placed at the site were directly connected with the gaseous
diffusion process, except for two boxes of specimens from Bettis Atomic
Power Laboratory (metal shapes clad with zirconium, zirconium alloy, or
hafnium) [DOE 58]. The waste buried at the site included a dismantled
INCO (International Nickel Company) Nickel Plant from Huntington, West
Virginia. The INCO plant was contaminated with nickel carbonyl and
uranium. (The plant had produced nickel in support of DOE’s three
enrichment plants.) [DOE 00a] The site also includes classified records,
compressor blades and other classified parts.
The facility was closed in 1994 with the construction of a multilayer
cap and a drainage system to capture surface water runoff. [Port 99c]
39) X-705 Salamanders (1950s-1970s)
Unsampled hydrocarbon-contaminated oils were burned in at least
"three 18-inch diameter salamander oil burners" on the west
side of X-705. DOE describes these devices as "trays, salamanders
(a primitive device consisting of an upright tube mounted on a
base)."
A 1973 Oak Ridge health protection appraisal found that "smoke
from the salamanders (believed to contain phosgene gas) was introduced
into the ventilation system [at X-705] and released into the X-705 high
bay."
A former employee indicated to DOE investigators that PCBs were
burned in the Salamanders. "The area where burning and spreading
occurred was covered with 10-12 inches of concrete. The spreading of
polychlorinated biphenyl (PCB) oil was then moved to area south of
X-326" [DOE 00a].
40) X-705A/B Incinerators (1950s-1986)
Beginning in the 1950s, two oil-fired incinerators burned waste: one,
"security burnables" and the other "uranium-contaminated
wastes generated from Plant operations." Former employees told DOE
that the latter burned solid and liquid wastes and "routinely
produced heavy black smoke." The two were replaced in 1971 by a
"pre-engineered" dual chamber incinerator installed in the
location of the uranium-contaminated waste incinerator, south of X-705.
The new incinerator, called by employees the "Radicator,"
burned materials from some one hundred locations at the plant [DOE 00a].
Between 1984 and 1986 the Radicator burned used oil and solvents,
materials that it was not equipped to handle and that, due to the
presence of cadmium and barium, come under RCRA. As a result Oak Ridge
ordered it to be shut down. The incinerator never restarted and was
closed under RCRA regulations in the 1990s [DOE 65]. The
incinerator and its structure were contaminated with radionuclides,
according to DOE’s 1993 report . Nearby soils were contaminated with
uranium, technetium 99, fluoranthene, and pyrene [DOE 1993].
Incinerator ash was sampled. If the ash contained sufficient uranium
for the uranium to be worth recovering, it was sent to the X-705 uranium
recovery facility. If not, it was usually boxed and placed in the X-749
landfill as long as it operated. Ash from the burning of floor sweepings
collected in areas where classified components were managed, was sent to
the X-749A classified landfill. [DOE 00a].
_____________________________________________________________________________________
*The
Uranium Enrichment Project is a project of Earth Island Institute’s
Yggdrasil Institute.
We are
grateful to The John Merck Fund for making possible our monitoring of
the US uranium enrichment establishment.
REFERENCES
BJ (Bechtel Jacobs Company), 2000, "Recycled Uranium Mass
Balance Project, Portsmouth, Ohio, Site Report," BJC/PORTS-139/R1,
Prepared by TetraTech NUS and Theta Technologies, Inc. under subcontract
23900-BA-ES008 for the US Department of Energy, Office of Environmental
Management, June 19.
DOE (US Department of Energy), 1987, "Environment, Safety, and
Health Office of Environmental Audit, Environmental Survey Preliminary
Report, Portsmouth Uranium Enrichment Complex," Piketon, Ohio,
August.
DOE (US Department of Energy), 1993a, "Report for Environmental
Audit Supporting Transition of the Gaseous Diffusion Plants to the
United States Enrichment Corporation," DOE/OR/10807&V2,
Appendix A, Volume I: Portsmouth Site Reports, June.
DOE (US Department of Energy), 1993b, "Report for Environmental
Audit Supporting Transition of the Gaseous Diffusion Plants to the
United States Enrichment Corporation," DOE/OR/1087&V3, Appendix
A, Volume II: Portsmouth Facilities Reports, June.
DOE (US Department of Energy), 1999a, "Programmatic
Environmental Impact Statement for Alternative Strategies for the
Long-Term Management and Use of Depleted Uranium Hexafluoride,"
DOE/EIS-0269, Office of Nuclear Energy, Science and Technology,
Germantown, Maryland, April.
DOE (US Department of Energy), 1999b, "Draft Environmental
Assessment: Disposition of Surplus Hanford Site Uranium, Hanford Site,
Richland, Washington," DOE/EA-1319, Richland Operations Office,
Richland, Washington, November.
DOE (US Department of Energy), 1999c, "Portsmouth Annual
Environmental Report for 1998," DOE/OR/11-3031, 2 volumes, Prepared
by EQ Midwest, Inc. under subcontract 23900-SC-SM002F for the US
Department of Energy, December.
DOE (US Department of Energy), 2000a, "Independent Investigation
of the Portsmouth Gaseous Diffusion Plant," 2 volumes, Office of
Oversight, Environment, Safety and Health, May.
DOE (US Department of Energy), 2000b, "Environmental Assessment:
Disposition of Surplus Hanford Site Uranium, Hanford Site, Richland,
Washington," DOE/EA-1319, Richland Operations Office, Richland,
Washington, June.
ERDA (Energy Research and Development Administration), 1977,
"Final Environmental Statement, Portsmouth Gaseous Diffusion Plant
Expansion, Piketon, Ohio," ERDA 1549, Vol. 2 of 2, September.
NRC (US Nuclear Regulatory Commission), 1999, "Compliance
Evaluation Report for the renewal of Certificate of compliance GDP-2,
Revision 1, United States Enrichment Corporation, Portsmouth Gaseous
Diffusion Plant, Piketon, Ohio," Docket 70-7002, January.
NUMERICAL LIST OF FACILITIES AND SITES INCLUDED
X-231A Oil
Biodegradation Plot #28
X-231B Oil
Biodegradation Plot #29
X-326
Process Building #3
X-300
Central Control Building #4
X-330
Process Building #2
X-333
Process Building #1
X-342 Feed
Vaporization and Fluorine Generation #5
X-343 Feed
Vaporization and Sampling #6
X-344 Feed
Manufacturing Plant #7
X-344A UF6
Sampling Facility #8
X-345
Special Nuclear Materials Storage #9
X-611A
Lime Sludge Lagoons #30
X-616
Liquid Effluent Control Facility #31
X-626-1
Recirculating Cooling Water #10
X-630-1
Recirculating Cooling Water #11
X-633-1
Recirculating Cooling Water #12
X-700
Maintenance Building #13
X-701B
Holding Pond #33
X-701C
Neutralization Pit and Pump Pit #32
X-705
Decontamination and Recovery #14
X-705
Salamanders #39
X-705A/B
Incinerators #40
X-710
Technical Services Building #15
X-710B
Building #16
X-720
Maintenance and Stores Building, #16a
X-734 Old
Sanitary Landfill #35
X-735
Sanitary Landfill #36
X-744G
Bulk Storage Warehouse #17
X-745
Cylinder Storage Yards #24
X-746 UF6
Sampling and Shipping Center #18
X-747H
Northwest Materials Storage #25
X-749
Contaminated Materials Disposal Facility #37
X-749A
Classified Materials Disposal Facility #38
X-749B
Peter Kiewit Landfill #34
X-760
Chemical Engineering Building #19
X-3001 Gas
Centrifuge Enrichment Plant Process Building #20
X-3002
GCEP Process Building #21
X-3346
GCEP Feed and Withdrawal #22
X-7725
GCEP Recycle/Assembly #23
A Hot Yard
#26
Small Hot
Yard --#27
copyright © 2000 by Mary Byrd Davis
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