Appropriate design and safety analyses were performed to demonstrate that:-the new steam generators are compatible with the existing plant,-that the plant can safely operate at higher power with adequate operating and safety margins.

This gave us the assurance that the steam generators for the Krsko Nuclear Power Plant were manufactured with the required quality and that they would operate safely and efficiently.

With this approach (shown in Fig. 1) all licensing issues (questions, concerns) were addressed and resolved in due time with the SNSA and should enable the authorized restart of the plant after the power uprating and SG replacement is authorized.

The results are maximum loads in terms of displacements and stresses during the analyzed period and response spectra for all lumped masses in the steam-generator model. The response spectra were used for seismic qualification of the new steam generators ([10] and [11]).

They are documented in a comprehensive set of reports which were used as the basis for the changes in the licensing documentation and were submitted to the SNSA in order to obtain an operational permit for the plant with he new steam generators and uprated power.

Take a suitable volume of the supernatant solution and adjust the pH to 6,5 by means of 1 M sodium hydroxide solution (4.8) with a pH-meter or with the bromocresol purple solution (4.10) as indicator. Evaporate to approximately half volume in a rotary evaporator at a temperature not exceeding 35 _C.

The TSOs from Ljubljana listed below were involved as independent reviewers supervision, quality assurance and quality control of the manufacturing process:-The Faculty of Mechanical Engineering,-The Welding Institute,-The Institute for Metal Structures,-The Institute of Metals and Technology.Their findings support the high technological level and the quality of the new steam generators.

Evaporator with a water bath for evaporation under reduced pressure;

a temperature-adjustable vaporization unit with a persilanized glass vapourizing element;

- temperature of evaporator:

Fit the column in the gas chromatograph, attaching the inlet end to the evaporator connected to the splitting system and the outlet end to the detector.

The capillary column is fitted inside the gas chromatograph by connecting the beginning of the column to the evaporator which is connected to the splitting system and the end of the column to the detector.

Evaporators for concentrated lithium hydroxide solution.

thermostatic vaporization assembly (injection port) with silanized coated glass;

The solvent is totally evaporated in air or in a rotary evaporator, and the thoroughly mixed material is added to the saturator column.

Heat exchangers (steam generators) specially designed or prepared for use in the primary coolant circuit of a "nuclear reactor";

Rotary film evaporator

a steam-generator;

Rotary vacuum evaporator, with a 500-ml round-bottom flask.

advice that the evaporator unit should be kept clean from thick layers of ice and that frequent defrosting facilitates the removal of the ice cover;

The manual shall specifically mention that sharp objects (such as knives, screwdrivers, etc. should not be used for removing ice as they could damage the evaporator unit.

the manual shall specifically mention that sharp objects (such as knives, screwdrivers, etc.) should not be used for removing ice as they could damage the evaporator unit;

Evaporate this fraction until it had just reached dryness by means of the rotary evaporator (4.3) at 60 °C.

Evaporate all the remaining ethyl acetate from the acid solution using a rotary film evaporator (2.4).

Evaporate until it had just reached dryness, under reduced pressure at 60 °C by means of the rotary evaporator (4.3).

Evaporate the methanol solution to dryness under reduced pressure at 40 C by means of a rotary film evaporator (4.3).

Evaporate the dichloromethane extract down to dryness on the rotary evaporator (4.2) operating under reduced pressure at 40° C.

Concentrate the eluate on the rotary evaporator at 40 °C to 50 °C until no more acetone is distilled.

From the eluate the solvents are distilled off on a rotatory evaporator at a water bath temperature of 40 to 50 °C.

Evaporate the methanol on the rotary film evaporator (4.2), the temperature of the waterbath should not exceed 40 °C.

Restore atmospheric pressure by admitting nitrogen (3.10) and remove the flask from the rotary evaporator.

Evaporate the solvent nearly to dryness on the rotary evaporator (4.1) with reduced pressure at a bath temperature not exceeding 40 °C.

CENTRIFUGE OR FILTER, TAKE 20 ML OF THE CLEAR SOLUTION AND EVAPORATE UNTIL DRY IN A ROTARY EVAPORATOR.

FOR CONTENTS OF LESS THAN 10 PPM, EVAPORATE THE EXTRACT UNTIL DRY IN A ROTARY EVAPORATOR AT 35* C AND DISSOLVE THE RESIDUE IN 40 % METHANOL.

Evaporate the latter almost to dryness at a temperature not exceeding 50 oC and under a stream of inert gas (3.11) with the rotary evaporator (4.5).

Elute aflatoxin B1 with 40 ml of the acetone-water mixture (3.5.1) and collect the whole of the eluate in the round bottomed flask of the rotary evaporator (4.4).

i. Heat exchangers (steam generators) specially designed or prepared for use in the primary coolant circuit of a "nuclear reactor";

Evaporate 100 ml of this extract on the rotary evaporator (see 5.4) nearly to dryness, remove the remaining solvent with a stream of nitrogen (3.10) and redissolve the residue in 10,0 ml of methanol (3.3).

advice that hot foodstuffs should be allowed to cool down before placing in the appliance, as the steam from the foodstuffs contributes to the icing up of the evaporator unit, but that the cooling period, however, should be as short as possible for health and hygiene reasons;

Evaporate the dichloromethane extract down to dyrness on the rotary evaporator (4.2) operating under reduced pressure at 40° C. Dissolve the residue in the flask with approximately 5 ml of methanol (3.2) and transfer this solution quantitatively to a 10 ml graduated flask.

"reversible air-conditioning/heat pump system" means a combination of interconnected refrigerant-containing parts constituting one closed refrigeration circuit, in which the refrigerant is circulated for the purpose of extracting and rejecting heat (i.e. cooling, heating), processes which are reversible in that the evaporators and condensers are designed to be interchangeable in their functions,

The carcases, originating from the slaughter floor, after chilling in refrigerating rooms operating with an air temperature at the outlet from the evaporators such that carcases can be cooled to an internal temperature of 7 °C within 48 hours for bovine carcases and 20 hours for sheep and pig carcases, are transported to the cutting premises, the temperature of which does not exceed 12 °C, located in the same group of buildings as the chillers.

The carcases, originating from the slaughterfloor, after chilling in refrigerating rooms operating with an air temperature at the outlet from the evaporators such that carcases can be cooled to an internal temperature of + 7 °C within 48 hours for bovine carcases and 20 hours for sheep and pig carcases, are transported to the cutting premises, the temperature of which does not exceed + 12 °C, located in the same group of building as the chillers.