The 12th International Conference on Environmental ... - Events
The 12th International Conference on Environmental ... - Events
The 12th International Conference on Environmental ... - Events
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Abstracts Sessi<strong>on</strong> 48<br />
As a result of this, a strategy for the simultaneous measurement of both Ce(IV) and Cr(VI) species in the presence of other i<strong>on</strong>s<br />
typically found in process streams (such as Ir<strong>on</strong>, Magnesium Neodymium and Aluminium) has been developed. <str<strong>on</strong>g>The</str<strong>on</strong>g> work presented<br />
will discuss the design and implementati<strong>on</strong> of the electrochemical techniques that we have used in the development of this strategy<br />
and in the measurement of the species in questi<strong>on</strong>.<br />
4) TREATMENT OF LIQUID RAW - TRIAL OPERATION OF FINAL TREATMENT CENTER MOCHOVCE - 16178<br />
Tibor Krajc, Milan Zatkulak, Marian Stubna, VUJE, a.s. (Slovakia); Vladimir Remias, JAVYS, a.s., (Slovaki)<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> Final Treatment Center (FTC) at Mochovce Nuclear Power Plant (NPP) has been introduced to trial operati<strong>on</strong> in 10/2007.<br />
One-year trial operati<strong>on</strong> of facility was planned. <str<strong>on</strong>g>The</str<strong>on</strong>g> Center is designed for treatment of liquid operati<strong>on</strong>al RAW and the treatment<br />
of radioactive wastes originated from decommissi<strong>on</strong>ing of NPP A-1 in Jaslovské Bohunice is tested, too.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> Center and processes parameters are described and a short descripti<strong>on</strong> of bituminisati<strong>on</strong> and cementati<strong>on</strong> technologies<br />
implemented to FTC including the auxiliary processes is given as well.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> time schedule of start-up and trial operati<strong>on</strong> phases is described and discussed. <str<strong>on</strong>g>The</str<strong>on</strong>g> amounts of treated wastes, the producti<strong>on</strong><br />
of waste packages and the balance of raw materials and energy c<strong>on</strong>sumpti<strong>on</strong> are displayed too.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> evaluati<strong>on</strong> of experience gained in the phase of Center trial operati<strong>on</strong> for bituminisati<strong>on</strong> processes (film evaporator process<br />
and the bituminisati<strong>on</strong> of resins) and the cement grouting is a part of this paper.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> identificati<strong>on</strong> of key interdependences within process parameters and treatment product properties and the fulfillment of<br />
the projected output parameters and required qualitative parameters of individual treated RAW products are displayed.<br />
5) RADIOACTIVE OIL DECONTAMINATION DEVELOPMENT — AN OVERVIEW - 16251<br />
John Krasznai, Kinectrics Inc. (Canada)<br />
Insulating, hydraulic and vacuum pump oils are used extensively in CANDU plants. It is inevitable that at some point in the<br />
equipment life cycle that these oils will become waste products and their disposal needs to be properly managed. <str<strong>on</strong>g>The</str<strong>on</strong>g> presence of<br />
radioactivity and c<strong>on</strong>venti<strong>on</strong>al c<strong>on</strong>taminati<strong>on</strong> in the oils (mixed waste) pose special challenges to the waste manager.<br />
This paper provides an overview of waste oil streams that have been problematic in the CANDU nuclear industry and the<br />
dec<strong>on</strong>taminati<strong>on</strong> processes that were developed for each to effectively remove a variety of radioactive species including tritium as<br />
well as c<strong>on</strong>venti<strong>on</strong>al hazardous materials such as PCB, lead and cadmium.<br />
6) INCINERATION OF CONTAMINATED OIL FROM SELLAFIELD - 16246<br />
Craig Broadbent, Studsvik UK Limited (UK); Helen Cassidy, Sellafield Limited (UK);<br />
Anders Stenmark, Studsvik Nuclear AB (Sweden)<br />
Studsvik have been incinerating Low Level Waste (LLW) at its licensed facility in Sweden since the mid-1970s. This process<br />
not <strong>on</strong>ly enables the volume of waste to be significantly reduced but also produces an inert residue suitable for final disposal. <str<strong>on</strong>g>The</str<strong>on</strong>g><br />
facility has historically incinerated <strong>on</strong>ly solid dry LLW, however in 2008 an authorisati<strong>on</strong> was obtained to permit the routine incinerati<strong>on</strong><br />
of LLW c<strong>on</strong>taminated oil at the facility.<br />
Prior to obtaining the authorisati<strong>on</strong> to incinerate oils and other organic liquids - both from clean-up activities <strong>on</strong> the Studsvik<br />
site and <strong>on</strong> a commercial basis - a development program was established. <str<strong>on</strong>g>The</str<strong>on</strong>g> primary aims of this were to identify the optimum<br />
process set-up for the incinerator and also to dem<strong>on</strong>strate to the regulating authorities that the appropriate envir<strong>on</strong>mental and radiological<br />
parameters would be maintained throughout the new process.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> final phase of the development program was to incinerate a larger campaign of c<strong>on</strong>taminated oil from the nuclear industry.<br />
A suitable accumulati<strong>on</strong> of oil was identified <strong>on</strong> the Sellafield site in Cumbria and a commercial c<strong>on</strong>tract was established to<br />
incinerate approximately 40 t<strong>on</strong>nes of oil from the site. <str<strong>on</strong>g>The</str<strong>on</strong>g> inventory of oil chosen for the trial incinerati<strong>on</strong> represented a significant<br />
challenge to the incinerati<strong>on</strong> facility as much of it had degraded following years of storage and was from various sources <strong>on</strong>site.<br />
In order to transport the c<strong>on</strong>taminated oil from the Sellafield site in the UK to the Studsvik facility in Sweden several challenges<br />
had to be overcome. <str<strong>on</strong>g>The</str<strong>on</strong>g>se included characterisati<strong>on</strong>, packaging and internati<strong>on</strong>al transportati<strong>on</strong> (under a Transfr<strong>on</strong>tier Shipment<br />
(TFS) authorisati<strong>on</strong>) for <strong>on</strong>e of the first transports of liquid radioactive wastes outside the UK.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> incinerati<strong>on</strong> commenced in late 2007 and was successfully completed in early 2008. <str<strong>on</strong>g>The</str<strong>on</strong>g> total volume reducti<strong>on</strong> achieved<br />
was greater than 97%, with the resultant ash packaged and returned to the UK (for ultimate disposal at the UK LLWR) in November<br />
2008.<br />
<str<strong>on</strong>g>The</str<strong>on</strong>g> paper will provide additi<strong>on</strong>al informati<strong>on</strong> <strong>on</strong> the characterisati<strong>on</strong>, packaging and incinerati<strong>on</strong> process as well as describe<br />
the nati<strong>on</strong>al and internati<strong>on</strong>al regulatory frameworks applicable to the project.<br />
7) SOLIDIFICATION OF RADIOACTIVE LIQUID WASTES, TREATMENT OPTIONS<br />
FOR SPENT RESINS AND CONCENTRATES - 16405<br />
Andreas Roth, Hansa Projekt Anlagentechnik GmbH (Germany)<br />
I<strong>on</strong> exchange is <strong>on</strong>e of the most comm<strong>on</strong> and effective treatment methods for liquid radioactive waste. However, spent i<strong>on</strong><br />
exchange resins are c<strong>on</strong>sidered to be problematic waste that in many cases require special approaches and pre-c<strong>on</strong>diti<strong>on</strong>ing during<br />
its immobilizati<strong>on</strong> to meet the acceptance criteria for disposal. Because of the functi<strong>on</strong> that they fulfill, spent i<strong>on</strong> exchange resins<br />
often c<strong>on</strong>tain high c<strong>on</strong>centrati<strong>on</strong>s of radioactivity and pose special handling and treatment problems.<br />
Another very comm<strong>on</strong> method of liquid radioactive waste treatment and water cleaning is the evaporati<strong>on</strong> or diaphragm filtrati<strong>on</strong>.<br />
Both treatment opti<strong>on</strong>s offer a high volume reducti<strong>on</strong> of the total volume of liquids treated but generate c<strong>on</strong>centrates which<br />
c<strong>on</strong>tain high c<strong>on</strong>centrati<strong>on</strong>s of radioactivity.<br />
Both menti<strong>on</strong>ed waste streams, spent resins as well as c<strong>on</strong>centrates, resulting from first step liquid radioactive waste treatment<br />
systems have to be c<strong>on</strong>diti<strong>on</strong>ed in a suitable manner to achieve stable waste products for final disposal.<br />
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