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title J01
source Learned and scientific writings
taken from Lancaster-Oslo-Bergen corpus of modern English (LOB) : [tagged, horizontal format] / Stig Johansson (http://ota.ox.ac.uk/desc/0167)
terms of use Distributed by the University of Oxford under a Creative Commons Attribution-NonCommercial-ShareAlike 3.0 Unported License.

1Unfortunately the accuracy with which an impurity dependent physical or chemical property of sodium can be measured decreases with decreasing impurity concentration .
2To get over this difficulty Alcock has suggested that instead of measuring directly the concentration of oxygen in the flowing sodium its thermodynamic potential should be measured by a suitable galvanic cell incorporated in the circuit .
3The principal advantages of this should be continuous monitoring of the sodium and an accuracy of monitoring which , if the sodium - oxygen system obeys Henry 's law , should increase with decreasing concentration of the impurity .
42 .
5Theoretical .
6( A ) .
7The cell .
8The use of solid electrolytes in galvanic cells has been described in detail by Kiukkola and Wagner .
9In a reversible cell consisting of two metal - metal oxide electrodes and a solid oxide electrolyte through which current is transported solely by 0<bsup>=<ast><bsup> ions , the change in free energy dg accompanying the passage of one mole of oxygen is given by : — 2EF where E is the voltage developed across the cell and F is the Faraday .
10If the electrodes are sodium saturated with its own oxide and unsaturated sodium the change of free energy accompanying the transfer of one mole of 0<bsup>=<ast><bsup> from the saturated to the unsaturated metal will be given by : — <ast><bcomment>formula<ast><ecomment> where <ast><bcomment>formula<ast><ecomment> , <ast><bcomment>formula<ast><ecomment> are the activities of oxygen in saturated sodium ( concentration c<bsub>0<ast><bsub> ) and in the unsaturated sodium ( concentration c < c<bsub>0<ast><bsub> ) , T the absolute temperature and R the gas - constant .
11If the activity of oxygen dissolved in sodium is proportional to its concentration as is required by Henry 's law then the free energy change per mole 0<bsup>=<ast><bsup> ion may be written <ast><bcomment>formula<ast><ecomment> .
12Thus <ast><bcomment>formula<ast><ecomment> .
13The solubility of oxygen as Na<bsub>2<ast><bsub>0 in sodium has been determined and is given by the relationship <ast><bcomment>formula<ast><ecomment> .
14Substitution of equation ( 3 ) in equation ( 2 ) with appropriate values for the various constants gives <ast><bcomment>formula<ast><ecomment> .
15Values of this function between 400 <deg> and 800 <deg> C at 100 <deg> intervals and for oxygen concentrations between 0.1 and 100 p.p.m are presented in fig 1 .
16At the present time maximum sodium coolant temperatures are around 500 <deg> C and oxygen concentrations are usually intended to be maintained in the range 1 - 10 p.p.m
17According to the above this cell under these conditions should give voltages ranging from 224 - 147 mv .
18( B ) .
19The effect of small changes of oxygen concentration and temperature on the cell E.M.F .
20The E.M.F of such a cell placed in a sodium circuit will be affected by fluctuations in oxygen content and temperature .
21These may be estimated from equation ( 4 ) or the following derived equations : — <ast><bcomment>formula<ast><ecomment> <ast><bcomment>formula<ast><ecomment> .
22Equation ( 5 ) indicates that any voltage fluctuation arising from a sudden small concentration change will be controlled principally by the original concentration .
23Thus changes from 0.1 to 1 p.p.m 1 - 10 p.p.m 10 - 100 p.p.m would result in the same change in voltage ( 1776 mv ) .
24For relevant reactor conditions ( 500 <deg> C , C = 1 - 10 p.p.m ) the finite change of voltage de accompanying finite concentration changes dc is plotted in fig 3 .
25The latter as might be expected vary considerably .
26A rise of oxygen concentration from 1 - 2 p.p.m is accompanied by a voltage drop of 1723 mv while , a rise from 9 - 10 p.p.m would produce a change of only 173 mv .
27Changes in voltage accompanying fluctuations of coolant temperature according to equation ( 6 ) vary only slightly with concentration and are proportional to the temperature change .
28Values at various oxygen concentrations of <ast><bcomment>formula<ast><ecomment> together with apparent changes in oxygen level for temperature fluctuations of 14 10 <deg> C at 500 <deg> C are presented in table 1 .
29The above figures show that a 14 10 <deg> C temperature fluctuation at oxygen levels in the range 1 - 10 p.p.m would indicate an apparent change of 1712 <percnt> in oxygen concentration .
30Providing a cell of the above type works satisfactorily the above arguments suggest that it will be sufficiently accurate as an oxygen monitor in a hot trapped sodium coolant circuit .
31( C ) .
32Contamination of the sodium circuit by oxygen from the cell .
33Experiments with solid oxide electrolyte galvanic cells have indicated that it is difficult to obtain reproducible voltages using normal potentiometric methods at temperatures below 750 <deg> C .
34The author has obtained reproducible results with such cells at 400 <deg> C and above by using vibrating reed voltmeters that draw current from the cell only as a result of leakage through insulation resistance of <ast><bcomment>formula<ast><ecomment> .
35Thus if voltmeters of this type were used with the Na <sol> Na<bsub>2<ast><bsub>0 cell it is possible to estimate the contamination of the circuit sodium from oxygen continuously diffusing through the electrolyte .
36If it is assumed that in practise the maximum voltage developed by the cell at 500 <deg> C will be around 300 mv ( see fig 1 ) then in the case of the instrument with the lower resistance the current will be : — 3 x 10<bsup> - 14<ast><bsup> coulombs <sol> sec .
37The charge on 0<bsup>=<ast><bsup> ion <ast>?183.2 x 10<bsup> - 19<ast><bsup> coulombs .
38Thus the number of 0<bsup>=<ast><bsup> ions travelling through the electrolyte per second <ast>?1810<bsup>5<ast><bsup> .
39The mass of oxygen per year at this rate would be approximately 8 x 10<bsup> - 1<ast><bsup> g <sol> year which is a quite insignificant quantity .
40( D ) .
41The use of the cell as a corrosion meter .
42With the cell electrodes consisting of sodium with oxygen at different activities a voltage will be developed that is a function of the difference in the oxygen potential at the two electrodes .
43Unless it is known at what oxygen potential a given material in the sodium coolant circuit will start to oxidise the cell can only be used as has been suggested above , as an oxygen concentration monitor .
44However , if a material oxidizes in sodium at a given oxygen potential the reference electrode could be held at that potential and oxidizing or reducing conditions in the coolant circuit for that material would be indicated by a negative or positive potential at the reference electrode .
45Thus for the specific case of niobium in a sodium circuit a corrosion indicator could be a reference electrode of sodium saturated and equilibrated with niobium separated from the coolant by a solid anionic electrolyte .
46A negative voltage from the reference electrode would mean oxidizing conditions for niobium and positive voltage , non - oxidizing conditions .
473 .
48Practical .
49The practical application of the above idea will involve considerable experimentation before it can be realised .
50The first requirement is for an anionic electrolyte , which can be fabricated into suitable shapes impervious to gases and liquid sodium and which is neither corroded by sodium nor by sodium monoxide .
51Possible materials are zirconia stabilised with lime and thoria doped with rare earth oxides .
52If such a material can be made with these properties a possible way in which the cell may be incorporated in a sodium circuit is depicted in fig 4 .
53The electrolyte A is made in the form of a thin walled closed off round end tube or probe fitting vertically into the sodium coolant circuit B .
54The <plus>ve electrode consisting of a small quantity of sodium saturated with sodium monoxide C is situated at the bottom of the tube .
55The potential acquired by this pool of sodium is transmitted to the voltmeter V by a nickel conductor D , nickel being resistant to corrosive attack by oxide saturated sodium at 500 <deg> C .
56The <minus>ve electrode which is the coolant stream , is joined to the voltmeter by an earthed nickel conductor attached to the bottom of a well E in the coolant stream .
57Provided the temperatures at C and E are the same , thermoelectric contributions to the voltage should be zero .
58The probe extends out of the sodium stream through a close fitting thin walled T - junction F and passes into the open via a water - cooled O ring seal G .
59The open end of the probe is sealed with a vacuum coupling H which also positions the <plus>ve nickel conductor with respect to the sodium by circlips on either side of the seal I .
60Evaporation of sodium from the pool C is minimised by a close fitting cylindrical block of electrolyte J attached to the <plus>ve nickel conductor by nickel circlips .
61Fixing and positioning of the probe relative to the coolant stream is effected by tie - bars of insulating material K joining the vacuum coupling H to the water cooled flange G .
62The probe can be evacuated and filled with inert gas via the tube L which must of course be electrically isolated after this has been carried out .
634 .
64Discussion .
65It is not suggested that the above proposal will be successful but rather that it is worth a trial in the event of the inadequacy of some simpler method of monitoring the oxygen in a sodium circuit .
66The principal difficulty encountered by the author , in determining partial molal free energies by solid electrolyte cells of very stable oxides such as UO<bsub>2<ast><bsub> , MnO etc was vapour phase transfer of oxygen by carbonaceous impurities in the blanket gas .
67This resulted in the oxidation of the <minus>ve electrode and reduction of the <plus>ve electrode which of course led to a loss in E.M.F from the cell .
68In the above design the two electrodes are completely separated from one another so that this major source of trouble should not be present .
69However , the stability of the system may be adversely affected by the thermal gradient up the probe and this can only be tested by experiment .
70Whether such an apparatus can be incorporated in a reactor circuit in a manner that will satisfy safety requirements will need further study .
71On the face of it however , there seems to be no reason why the cell should not be double - contained to prevent loss of sodium in the event of the ceramic tube being fractured .
72Such containment however , will be complicated by the necessity of providing suitable insulating seals through its walls .
735 .
74Conclusions .
75If other monitoring methods for oxygen in sodium in the concentration range 1 - 10 p.p.m are found to be inadequate then this galvanic cell may be worth investigating .
76However , it will require development of a suitable electrolyte and even then it will only be useful if the activity of the dissolved oxygen varies sufficiently with changes in its concentration .
77A .
78Outline of method .
79To a measured portion of the sample , niobium and zirconium carriers are added together with hydrofluoric acid to ensure complete isotopic interchange .
80Rare earth elements are co - precipitated with lanthanum as fluorides .
81Niobium is precipitated with ammonia , partially separating it from zirconium .
82The niobium precipitate is dissolved in a mixture of oxalic and nitric acids , and niobic acid precipitated by boiling and adding potassium bromate .
83The niobic acid is dissolved in acid ammonium fluoride and the cycle from the ammonia precipitation repeated .
84The niobic acid is washed , ignited to niobium pentoxide , which is mounted on a tared counting tray and weighed .
85The g - activity is measured through a lead <sol> aluminium sandwich using standard gamma scintillation equipment , which has been calibrated with known amounts of niobium - 95 .
86B .
87Reagents required .
88All reagents are analytical reagent quality where available .
891 .
90Standard niobium carrier solution ( <ast><bcomment>formula<ast><ecomment> ) .
91Fuse 20 g of pure niobium pentoxide with 72 g of potassium carbonate in a platinum dish .
92Cool and dissolve the solidified melt in about 400 ml of hot water .
93Transfer the solution and any undissolved solid to a glass beaker , stir thoroughly and add 16 M nitric acid until the solution is strongly acid to litmus .
94Stand the beaker on a hot plate and keep the solution warm for 30 minutes to coagulate the precipitate .
95Transfer to four 200 ml polythene bottles , centrifuge , decant and discard each supernate .
96Wash each portion of the precipitate three times by stirring with 100 ml of 2 <percnt> ammonium nitrate .
97Use a glass rod for stirring .
98Centrifuge and discard the supernates after each wash .
99Dissolve each portion of the precipitate in 25 ml of 30 <percnt> ammonium fluoride and 15 ml of 16 M nitric acid .
100Combine the solutions from each of the 200 ml polythene bottles , and dilute to 2 litres with distilled water in a polythene bottle .
101Standardize as follows : —
102Pipette 10 ml of the solution into a 400 ml polythene beaker and add 100 ml of a saturated solution of ammonium chloride .
103Heat the solution nearly to boiling , by placing the polythene beaker in a glass beaker of water , heated on a hot plate , and add to the solution 1 g of tannic acid dissolved in hot water .