Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities
The paper presents the analytical and experimental studies of the process of cadmium and zinc refinement of interstitial impurities in a vacuum using a getter filter of Zr-Fe alloy. The thermodynamic analysis of reduction reactions of cadmium, zinc, carbon oxides, and zinc nitride with getter materi...
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Національний науковий центр «Харківський фізико-технічний інститут» НАН України
2014
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Цитувати: | Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities / A.I. Kondrik, G.P. Kovtun, A.P. Shcherban’, D.A. Solopikhin // Вопросы атомной науки и техники. — 2014. — № 1. — С. 32-36. — Бібліогр.: 12 назв. — анг. |
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irk-123456789-799212015-04-09T03:01:51Z Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities Kondrik, A.I. Kovtun, G.P. Shcherban’, A.P. Solopikhin, D.A. Чистые материалы и вакуумные технологии The paper presents the analytical and experimental studies of the process of cadmium and zinc refinement of interstitial impurities in a vacuum using a getter filter of Zr-Fe alloy. The thermodynamic analysis of reduction reactions of cadmium, zinc, carbon oxides, and zinc nitride with getter material of Zr-Fe alloy, depending on the temperature and vacuum conditions of the metals refining process have been accomplished. The experiments showed the effectiveness to use the Zr (51)-Fe (49) wt. % alloy getter filter for Cd and Zn refinement of interstitial impurities. Представлены аналитические и экспериментальные исследования процесса рафинирования кадмия и цинка в вакууме с применением геттерных фильтров из сплава Zr-Fe от примесей внедрения (C, N, O). Выполнен термодинамический анализ восстановительных реакций оксидов кадмия, цинка, углерода и нитрида цинка с материалом геттера из сплава Zr-Fe в зависимости от температуры и вакуумных условий проведения процесса рафинирования этих металлов. Экспериментально показана эффективность применения геттерного фильтра из сплава Zr(51)-Fe(49) мас.% для очистки Cd и Zn от примесей внедрения. Представлені аналітичні та експериментальні дослідження процесу рафінування кадмію та цинку у вакуумі із застосуванням гетерних фільтрів зі сплаву Zr-Fe від домішок проникнення (C, N, O). Виконанo термодинамічний аналіз відновних реакцій оксидів кадмію, цинку, вуглецю і нітриду цинку з матеріалом гетера зі сплаву Zr-Fe в залежності від температури та вакуумних умов проведення процесу рафінування цих металів. Експериментально показана ефективність застосування гетерного фільтра зі сплаву Zr (51)-Fe (49) мас.% для очищення Cd і Zn від домішок проникнення. 2014 Article Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities / A.I. Kondrik, G.P. Kovtun, A.P. Shcherban’, D.A. Solopikhin // Вопросы атомной науки и техники. — 2014. — № 1. — С. 32-36. — Бібліогр.: 12 назв. — анг. 1562-6016 http://dspace.nbuv.gov.ua/handle/123456789/79921 669.054 en Вопросы атомной науки и техники Національний науковий центр «Харківський фізико-технічний інститут» НАН України |
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Digital Library of Periodicals of National Academy of Sciences of Ukraine |
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Чистые материалы и вакуумные технологии Чистые материалы и вакуумные технологии |
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Чистые материалы и вакуумные технологии Чистые материалы и вакуумные технологии Kondrik, A.I. Kovtun, G.P. Shcherban’, A.P. Solopikhin, D.A. Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities Вопросы атомной науки и техники |
description |
The paper presents the analytical and experimental studies of the process of cadmium and zinc refinement of interstitial impurities in a vacuum using a getter filter of Zr-Fe alloy. The thermodynamic analysis of reduction reactions of cadmium, zinc, carbon oxides, and zinc nitride with getter material of Zr-Fe alloy, depending on the temperature and vacuum conditions of the metals refining process have been accomplished. The experiments showed the effectiveness to use the Zr (51)-Fe (49) wt. % alloy getter filter for Cd and Zn refinement of interstitial impurities. |
format |
Article |
author |
Kondrik, A.I. Kovtun, G.P. Shcherban’, A.P. Solopikhin, D.A. |
author_facet |
Kondrik, A.I. Kovtun, G.P. Shcherban’, A.P. Solopikhin, D.A. |
author_sort |
Kondrik, A.I. |
title |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities |
title_short |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities |
title_full |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities |
title_fullStr |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities |
title_full_unstemmed |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities |
title_sort |
influence of zr-fe getter filter on cd and zn deep refining of interstitial impurities |
publisher |
Національний науковий центр «Харківський фізико-технічний інститут» НАН України |
publishDate |
2014 |
topic_facet |
Чистые материалы и вакуумные технологии |
url |
http://dspace.nbuv.gov.ua/handle/123456789/79921 |
citation_txt |
Influence of Zr-Fe getter filter on Cd and Zn deep refining of interstitial impurities / A.I. Kondrik, G.P. Kovtun, A.P. Shcherban’, D.A. Solopikhin // Вопросы атомной науки и техники. — 2014. — № 1. — С. 32-36. — Бібліогр.: 12 назв. — анг. |
series |
Вопросы атомной науки и техники |
work_keys_str_mv |
AT kondrikai influenceofzrfegetterfilteroncdandzndeeprefiningofinterstitialimpurities AT kovtungp influenceofzrfegetterfilteroncdandzndeeprefiningofinterstitialimpurities AT shcherbanap influenceofzrfegetterfilteroncdandzndeeprefiningofinterstitialimpurities AT solopikhinda influenceofzrfegetterfilteroncdandzndeeprefiningofinterstitialimpurities |
first_indexed |
2025-07-06T03:51:21Z |
last_indexed |
2025-07-06T03:51:21Z |
_version_ |
1836868049964105728 |
fulltext |
32 ISSN 1562-6016. ВАНТ. 2014. №1(89)
UDC 669.054
INFLUENCE OF Zr-Fe GETTER FILTER ON Cd AND Zn DEEP
REFINING OF INTERSTITIAL IMPURITIES
A.I. Kondrik, G.P. Kovtun, A.P. Shcherban’, D.A. Solopikhin
National Science Center «Kharkov Institute of Physics and Technology»,
Kharkov, Ukraine
E-mail: kondrik@kipt.kharkov.ua
The paper presents the analytical and experimental studies of the process of cadmium and zinc refinement of in-
terstitial impurities in a vacuum using a getter filter of Zr-Fe alloy. The thermodynamic analysis of reduction reac-
tions of cadmium, zinc, carbon oxides, and zinc nitride with getter material of Zr-Fe alloy, depending on the tem-
perature and vacuum conditions of the metals refining process have been accomplished. The experiments showed
the effectiveness to use the Zr (51)-Fe (49) wt. % alloy getter filter for Cd and Zn refinement of interstitial impuri-
ties.
INTRODUCTION
High-purity source metals Cd and Zn are composite
components of many compound semiconductor and
scintillation materials. Multi-semiconductor (CdTe,
CdZnTe), and scintillation single crystals (CdWO4,
ZnWO4, CdMoO4, ZnMoO4, ZnSe) will be applied to
the manufacture of ionizing radiation detectors [1], low-
background scintillators for registration of various elec-
tromagnetic radiations, including that rare events, such
as neutrinoless double beta-decay of nuclei and registra-
tion of dark matter particles [2], which at the present
time have a greater interest. For the synthesis of high-
quality detector materials the purity of the source zinc
and cadmium should be not less than
99.9999…99.99999%, at that the concentration of each
of the metallic impurity full range (up to 80 elements) is
not more than 1·10-6 wt.%, including the interstitial im-
purities fraction (C, N, O) should be at the level of
1·10-5 wt.%. Therefore, due to the strong demands to the
purity of the source components across the full range of
impurity elements it is necessary to take into account all
the requirements for the pure material during prepara-
tion of high-purity Cd and Zn. It requires the research
and development of new approaches to the processes of
the metals deep refining.
During the development of effective removal of in-
terstitial impurities it is important to know their behav-
ior in metals in terms of thermodynamics. This informa-
tion is essential for selection of technological conditions
of the purification process.
1. PROBLEM
The purity of the refined cadmium and zinc are
mainly limited by the concentration of residual intersti-
tial impurities [3]. Removing them from the metals is
difficult due to the formation of strong bonds of these
impurities with the substrate. Typical content of intersti-
tial impurities in high-pure Cd and Zn is at least
5·10-2...5·10-3 wt.%, while the removal of metal impuri-
ties to the concentration < 1·10-5 wt.% may be achieved
by conventional distillation methods of refinement.
Vacuum distillation is the best method for removal of
gaseous impurities from the reactive metals, since in
this case there is a decrease of oxidation and gas absorp-
tion. Oxygen and carbon, as a rule, are not removed
from the metal in the atomic state, but rather in form of
compounds, however during distillation in vacuum it is
necessary to combine the evaporation and condensation
with reducing reactions that may be performed by using
chemically active getter filters.
When selecting the getter material to clean the Cd
and Zn, the following requirements to getter have been
taking into account: high reactivity to gas impurities (H,
N, O) and carbon-containing gases; no interaction of
getter with the Zn and Cd vapors; low values of the get-
ter material vapor pressure at the temperature of use,
high sorption capacity at the operating temperature of
distillation (690...810 K).
Sorption properties of a number of chemically active
metals, intermetallic compounds and alloys based on
zirconium and hafnium have been investigated previ-
ously in KIPT [4, 5]. These materials are suitable for the
operating temperature of 500...800 K and can be repeat-
edly used after the relevant activation.
As follows from [4], high sorption properties inher-
ent in the alloys of zirconium and hafnium with iron.
Zr-Fe alloy was selected as the material for getter filter
recommended to remove interstitial impurities from Cd
and Zn, due to its high sorption characteristics, ease of
production and relatively low cost.
The aim of this study is to investigate the processes
of separation of Cd and Zn from interstitial impurities
by means of vacuum distillation method using Zr-Fe
getter filter as a reductant.
2. ANALYSIS AND EXPERIMENTAL STUDY
OF DEEP CLEANING CADMIUM AND ZINC
At the initial purification stage the removal of car-
bon and oxygen occurs as volatile compounds with oth-
er impurities and depends on their proportions. With
increasing the metal purity the oxygen, carbon and ni-
trogen, forming strong bonds with a base in the form of
oxides, carbides, nitrides, are often become as residual
impurities which are difficult to remove. Evaporating
metal may also form compounds with atoms and mole-
cules of the gaseous environment. If formed compounds
are stable, the impurity may get into the distillate. Thus,
during deep refining of metals it should be pay attention
to the behavior of stable oxides, carbides and nitrides.
Let us consider the behavior of interstitial impurities in
Cd and Zn firstly for the example of oxygen.
ISSN 1562-6016. ВАНТ. 2014. №1(89) 33
To assess the effect of vacuum on the stability of ox-
ides the standard Gibbs energy change
0
MeOGΔ may be
used for the reaction of metal oxide formation, adjusted
by the amount that takes into account the transition to a
gaseous state at a pressure P. Distillation of Cd and Zn
in vacuum may be carried out at the temperature T~
0.6· МеО
boilT , where МеО
boilT is the boiling temperature of
metal under atmospheric pressure.
For the case where the activity of MeO is equal to 1
as well as
Ме
boilT <
МеО
boilT the oxygen potential of forma-
tion of bivalent metal solid oxide ΔGMeO is given by
PRTGG MeOMeO ln20 −Δ=Δ , (1)
where 0
MeOGΔ is the standard Gibbs energy change for
the reaction of the metal oxide formation; T is the
temperature of process, K; P is the vapor pressure of the
metal, bar; R is the universal gas constant.
The processes of vacuum evaporation of cadmium,
zinc and oxygen impurity are characterized by the reac-
tions of formation and decay of the metals oxides. Zinc
forms in the condensed and gaseous states the monoxide
ZnO [6], the reaction of formation of which is as fol-
lows:
2Zn(gas) + O2 = 2ZnO.
Cadmium forms a stable oxide CdO, existing in a
condensed and gaseous states. The formation reaction of
cadmium oxide is given by
2Cd(gas) + O2 = 2CdO.
Let us estimate the stability change of the oxides
with a temperature and under different vacuum condi-
tion. For the distillation of zinc at the temperatures
above the boiling point (1180 K), the oxygen potential
of ZnO with taking into account (1) will be written as
follows:
510013.1
lg3.3822.375910012
⋅
⋅−⋅+−=Δ
PTTGZnO , (2)
where T is the temperature of process, K; P is the vapor
pressure of the metal (zinc), Pa.
However, due to the strong evaporation of zinc in
vacuum even at T = 730...870 K, it was possible to carry
out the distillation at these temperatures and extrapolate
the expression (2) on this area, because here we have a
Zn vapor phase also. In this temperature range ZnO
exists in the solid state, which allows using the formulas
(1), (2). Oxygen molecules and atoms of zinc vapors get
in the getter filter and they can form there oxide, there-
fore it is necessary to compare the ΔGZnO for formation
of oxide ZnO with ΔGMeO for the formation of getter
components oxides within operation ranges of tempera-
ture and pressure of gaseous medium. Molecules ZnO,
formed in the vapor phase, can also reach to getter by
means of carrying away them with intensely evaporat-
ing Zn atoms under vapor pressure of zinc
~ 133…13.3 Pa. A similar physical model can be as-
sumed to study the stability of CdO.
Oxygen potential of CdO is given by
510013.1
lg3.3824.399722426
⋅
⋅−⋅+−=Δ
PTTGCdO . (3)
The Gibbs energy change applied to nitrides forma-
tion can be considered for impurity N. Zinc reacting
with nitrogen and forms relatively stable chemical com-
pound Zn3N2 which is characteristic one for elements of
group IIA [7]. According to experimental data the com-
pound Zn3N2 is stable up to 623 K in a vacuum and up
to 773 K in air environment, and the solubility of nitro-
gen in zinc is low.
Nitrogen can form a cadmium nitride Cd3N2 which
decomposes at a temperature close to the Cd melting
point, and the generated nitrogen gas can be removed
from the system without getter. The solubility of nitro-
gen in cadmium was not discovered up to the tempera-
ture of 673 K [7].
Zinc carbide ZnC2 may be formed in systems Zn-C
and Cd-C, but this compound can be obtained by chem-
ical synthesis only. The solubility of carbon is low in
cadmium and zinc at the temperatures of evaporation.
Gas release from cadmium and zinc occurs in the form
of CO and CO2 during heating in vacuum. Separation of
cadmium and zinc from the carbon during distillation
using the getter filter can be carried out by means of the
reduction of the CO volatile compound to form zirco-
nium and iron oxides. Partial pressure P(CO) and
P(CO2) are assumed to be small compared to the total
pressure in the system, which is determined by the metal
vapors.
Thus, let’s consider from the thermodynamics aspect
the Cd and Zn refining of interstitial impurities during
vacuum distillation using Zr-Fe getter filter for the ex-
amples of reducing CdO, ZnO, Zn3N2, CO, CO2.
Fig. 1 shows the dependences of the Gibbs energy
change per 1 mole of oxygen for the formation of ZnO
and other oxides vs temperature under different pressure
of the gaseous environment in the system. Similar de-
pendences are shown for the formation of CdO (Fig. 2)
and Zn3N2 (Fig. 3). It is seen from figures 1 and 2 that
the stability of CdO and ZnO decreases with increasing
system temperature and with decreasing pressure. To
decompose ZnO under atmospheric pressure the re-
quired temperatures is in excess of 2300 K, whereas at
the pressure of 1.33 Pa this oxide is instable at
T > 1620 K, and at pressure P = 1.33·10-2 Pa that does at
T > 1470 К. A similar pattern is observed for CdO and
differs only by the lower temperature of decomposition.
It can be seen from Fig. 3 that at the zinc distillation
operating temperatures (733...793 K) Zn3N2 compound
is unstable under a pressure of 133 Pa in the system.
If temperature and pressure in the system during the
metal distillation is insufficient for the decay of oxide
then the reduction of metals from oxides MeO using
reducing agent can be used for refining. Reduction reac-
tion scheme is as follows:
, MeOMeMeMeO IIII +=+ (4)
where MeII is the reducing metal.
Hard alloy Zr-Fe was selected as a metal reducing
agent. Zirconium has a much greater chemical affinity
for oxygen than iron. In the condensed state for the con-
ditions under consideration it was established the exis-
tence of only one stable oxide – ZrO2, the formation
reaction of which and Gibbs energy change are as fol-
lows [6, 8]:
34 ISSN 1562-6016. ВАНТ. 2014. №1(89)
Zr + O2 = ZrO2, T = 298…2123 K,
⎟
⎠
⎞
⎜
⎝
⎛
⋅
⋅−⋅+−=Δ 5
2
10013.1
)(lg15.198.1831092754
2
OPTTGZrO . (5)
In the formula (5) P (O2) is the partial pressure of
oxygen in the system.
Figs. 1 and 2 shows the Gibbs energy changes for
the reaction of zirconium dioxide formation. The graphs
show that the reduction of CdO and ZnO by zirconium
may easily been performed from thermodynamics as-
pect within the entire investigated range of temperatures
and pressures. However, the feasibility of the reaction
does not guarantee its active behavior. Since in our case
the distillation of cadmium and zinc is carried out at low
temperatures, it may well be that the local temperature
of the reactants is not enough for a quick reaction. In the
steel industry to enhance metallothermic reducing the
reacting system is often introduced with easily reducible
oxides, that provide additional heat contributing to an
increase in temperature of the reactants. For example,
the easily reducible oxide Fe3O4 is added in the charge
during production of titanium by aluminothermic reduc-
tion of TiO2, and for 100 g TiO2 it is required 83g Fe3O4
[8]. In this regard, one can expect an increased separa-
tion efficiency of Cd and Zn from oxygen and nitrogen
by carrying out the reducing reaction with zirconium in
the presence of iron oxide.
450 500 550 600 650 700 750
-900000
-800000
-700000
-600000
-500000
-400000
-300000
-200000
ΔGMeO, J/mol FeO
Fe3O4Fe2O3 0,0133
0,133
1,33
13,3
133
105
ZrO2
Temperature, ОC
P, Pa
ZnO
Fig. 1. Gibbs energy change for ZrO2, Fe2O3 formation
under oxygen partial pressure 0.00133 Pa, as well as
for ZnO in depending on temperature under different
pressure of metal vapor in the system:
105; 133; 13.3; 1.33; 0.133; 0.0133 Pa
Iron is easily oxidized in an oxidizing atmosphere to
form FeO, Fe3O4 and Fe2O3. The following formation
reaction of Fe2O3 occurs [6, 8] in the conditions under
consideration:
322 O2Fe = 3O + 4Fe , Т = 298…1809 К,
.
10013.1
)(133lg15.199.165542916Δ 5
2
32
⎟
⎠
⎞
⎜
⎝
⎛
⋅
⋅
⋅−⋅+=
OPTT-G OFe
(6)
Our preliminary experiments showed a higher de-
gree of Cd and Zn refining from impurities by distilla-
tion with getter of Zr-Fe, as compared with distillation
by getter of pure Zr. Separation of metals from oxygen
can progress as follows. Oxygen passes from Cd or Zn
to Zr and Fe according to three reactions (4)–(6), at that
in (4) MeII and MeIIO correspond to Zr (Fe) and ZrO2
(Fe2O3), and MeO corresponds to CdO or ZnO. In addi-
tion, the transition of the source oxygen from iron oxide
to zirconium oxide may be carried out by means of re-
duction of iron oxide with zirconium according to reac-
tion scheme (4), that accompanied with heat release and
increase of getter temperature, which should activate the
reducing reaction of the metal from CdO and ZnO, as
well as reaction (5) and (6). A similar outline can be
proposed for the Zn purification of nitrogen.
The real means of Cd and Zn purification of carbon
using a getter may be the reduction of C from volatile
compound CO emitted from the Cd and Zn matrix by
the use of filter Zr-Fe to form zirconium oxide with
releasing of solid carbon on the getter surface. Condi-
tion of carbon reduction is the higher getter metal affin-
ity to oxygen than carbon that to oxygen. Chemical af-
finity of zirconium and iron to oxygen is estimated in
accordance with formulas (5) and (6), and affinity of
carbon to oxygen – according to the change of Gibbs
energy ΔGC/CO for reaction: 2C + O2 = 2CO. The for-
mula for calculating the ΔGC/CO is:
( )⎟
⎟
⎠
⎞
⎜⎜
⎝
⎛
⋅⋅
⋅+⋅−−=Δ
2
5/ 10013.1
lg3.3817975221120
OP
P
TTG CO
COC , (7)
where PCO is the partial pressure of CO, Pa. Formula (7)
is valid for the case where the activity of carbon is equal
to 1. Oxygen partial pressure in the system is assumed
to be equal 0.00133 Pa. We also assume that under con-
dition of vacuum distillation the volatile compound CO
does not react with vapors of zinc, cadmium, and mole-
cules of gaseous medium. With origin of carbon reduc-
tion at T > 773 K it is possible to involve the volatile
compound CO2 into purification process according to
the reaction: C + CO2 = 2CO.
Temperature dependence of the Gibbs energy
change for the reactions of iron oxides formation are
shown in Figs. 1, 2, and those for the reaction of iron
nitrides formation – in Fig. 3. It follows from Fig. 2, the
reduction of CdO in accordance with the above scheme,
using a getter filter Zr-Fe, is possible within the whole
considered intervals of temperatures and pressures.
As can be seen from Figs. 1 and 3, participation of
iron in the process of ZnO reduction is possible under
ultrahigh vacuum only, and that in the process of Zn3N2
reduction – under a system pressure of not less than
0.0133 Pa at the temperature interval 753...793 K.
Fig. 3 also shows that the compound Zn3N2 may be de-
composed under high vacuum at elevated temperatures
of distillation.
The compounds Fe4N and Fe8N are also unstable at
the operating temperatures of zinc distillation
753…793 К, but the separation of zinc from nitrogen by
means of vacuum distillation using a getter may be car-
ried out according to the same outline as the removal of
oxygen.
Zn3N2 decomposition and removal of releasing
gaseous nitrogen from the system should prevail under
conditions of elevated temperature and high vacuum.
Fig. 4 shows the temperature dependences of the Gibbs
free energy change to form CO in accordance with the
reaction 2C + O2 = 2CO under different CO partial
pressure in the system, and to form Fe2O3 and ZrO2
also.
ISSN 1562-6016. ВАНТ. 2014. №1(89) 35
340 360 380 400 420 440 460 480 500 520
-900000
-800000
-700000
-600000
-500000
-400000
-300000
-200000
ΔGMeO, J/mol
Temperature, ОС
CdO
P, Pa
105
133
13,3
1,33
0,133
0,0133
ZrO2
Fe2O3
Fig. 2. Gibbs energy change for the formation of CdO
depended on the temperature under different pressures
of metallic vapors in the system, as well as for forma-
tion of ZrO2 and Fe2O3 under partial oxygen pressure
0.00133 Pa
440 460 480 500 520 540 560 580 600 620
-600000
-500000
-400000
-300000
-200000
-100000
0
100000
200000
Fe4N
1,33
133
13,3
0,133
P, Pa
Temperature, OC
ΔG, J/mol
Zn3N2
ZrN
0,0133
760
Fe8N
Fig. 3. Gibbs free energy change for the Zn3N2
formation under different metal vapor pressure in the
system 1.013·105; 133; 13.3; 1.33; 0.133; 0.0133 Pa
and for the formation of nitrides of zirconium and iron
under the partial pressure of nitrogen 0,00133 Pa
The dependence of the standard Gibbs energy
change for the formation of CO2 is shown also for
comparison. The figure shows that only zirconium can
directly participate in the process of separation of
distilling metal from oxygen by means of carbon
reduction from volatile compound CO.
Performed thermodynamic analysis of redox
reactions of the oxides of cadmium, zinc and carbon
with the getter alloy Zr-Fe yielded initial data to select
optimal temperature and vacuum conditions for metals
deep refining of interstitial impurities.
350 400 450 500 550 600
-900000
-800000
-700000
-600000
-500000
-400000
-300000
CO2
Fe2O3
ZrO2
1,33.10-10
1,33.10-8
0,0133
1,33
105
PCO
, Pa
ΔG, J/mol
Temperature, OС
CO
Fig. 4. Gibbs free energy change to form CO at different
partial pressure of CO as well as CO2 under
atmospheric pressure of CO2, and for the formation of
oxides ZrO2, Fe2O3 under a partial oxygen pressure
0,00133 Pa
Refining of cadmium and zinc using the getter filter
of Zr(51)-Fe(49) wt.% alloy was performed using
previously developed device and method described in
[9-12]. The process of Cd and Zn refinement using the
Zr-Fe filter was carried out in quasi-closed system
placed in a chamber under the pressure (2.7…5.3)·10-3
Pa, and at the evaporation temperatures of cadmium
653…693 К and zinc 753…793 К. The source materials
for the refining were Kd0A technical purity grade
cadmium (State Standard 1467-93) and brand TSV00
zinc ingots (State Standard 3640-94).
Efficiency of separation from interstitial impurities
using a getter filter provided in the table. The table
shows that proposed method with use of getter filter
provides a more effective cadmium and zinc
purification of gaseous impurities and carbon (distillates
II) as compared with purification without filter. The
degree of refinement using getter is more than tenfold
whereas refining efficiency without getter is 3...5 fold,
as compared with impurity content of the source metal.
The analysis showed at that, there was an additional
(2...5 times) separation from the main metallic
impurities compared with the content of these impurities
in the distillates produced without a filter.
Content of C, O, N impurities in cadmium and zinc after distillation using getter filter of Zr (51)-Fe (49) wt.%
Impurity content, ×10–4 wt.%
In refining metal Metal Impurities In source metal distillate I (no getter) distillate II (with getter filter)
C 20 6 < 1
N 5 1 < 1
O 45 10 < 1 Cd
*Σвнд 70 17 < 3
C 80 20 < 1
N 20 6 < 1
O 25 14 < 1 Zn
*Σвнд 125 40 < 3
36 ISSN 1562-6016. ВАНТ. 2014. №1(89)
*Σвнд is the total content of interstitial impurities.
The table also shows that the use of the getter
provides a slightly more effective removal of impurities
from Zn compared with Cd. It is due to the higher
stability of ZnO and Zn3N2 as compared with CdO and
Cd3N2 respectively. In other words, the more stable the
compound formed with interstitial impurity, the stronger
the influence getter filter for removal of the impurities.
This confirms the validity of initial assumptions
about the effect of the stability of considered com-
pounds on the concentration of residual interstitial im-
purities. Comparison of Figs. 1-4 with the data in the
table suggests that iron plays only a role of catalyst in
the zinc reduction reactions. In cadmium Fe may also
directly participate in the process of CdO reduction with
a subsequent transition of oxygen impurity from Fe2O3
to ZrO2. Fe may participate also in separation of gas
medium from molecular oxygen during the Cd
distillation.
Quantitative analysis of impurities in initial and
refined samples of cadmium and zinc were determined
by spark mass spectrometry – SMS (Giredmet,
Moscow, Russia). The error of analysis results by this
method is characterized by the relative standard
deviation of 0.15...0.30.
CONCLUSIONS
The optimal conditions to carry out the processes of
cadmium and zinc deep refining of the interstitial
impurities are determined basing on the analysis.
Iron is only a catalyst for redox reactions involving
Zr during distillation of Zn and Cd. Activating
metallothermic reduction is due to the heat released in
the reducing reaction: Fe2O3 + Zr → ZrO2 + Fe and
subsequent rise of getter temperature.
A refining method using a getter filter of Zr-Fe alloy
enables more efficient removal of interstitial impurities
compared with distillation without filter. Their content
has decreased more than tenfold as compared with the
concentration in the source metals.
The more stable compound with C, O, N, the greater
the effect of getter filter on removal of these impurities.
An important factor affecting the concentration of
residual interstitial impurities and ultimate purity of Cd
and Zn is the stability of ZnO, CdO, Zn3N2, CO, CO2.
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Статья поступила в редакцию 10.07.2013 г.
ВЛИЯНИЕ ГЕТТЕРНОГО ФИЛЬТРА Zr-Fe НА ГЛУБОКУЮ ОЧИСТКУ Cd И Zn
ОТ ПРИМЕСЕЙ ВНЕДРЕНИЯ
А.И. Кондрик, Г.П. Ковтун, А.П. Щербань, Д.А. Солопихин
Представлены аналитические и экспериментальные исследования процесса рафинирования кадмия и цинка в вакуу-
ме с применением геттерных фильтров из сплава Zr-Fe от примесей внедрения (C, N, O). Выполнен термодинамический
анализ восстановительных реакций оксидов кадмия, цинка, углерода и нитрида цинка с материалом геттера из сплава
Zr-Fe в зависимости от температуры и вакуумных условий проведения процесса рафинирования этих металлов. Экспе-
риментально показана эффективность применения геттерного фильтра из сплава Zr(51)-Fe(49) мас.% для очистки Cd и
Zn от примесей внедрения.
ВПЛИВ ГЕТЕРНОГО ФІЛЬТРА Zr-Fe НА ГЛИБОКЕ ОЧИЩЕННЯ Cd ТА Zn
ВІД ДОМІШОК ПРОНИКНЕННЯ
О.І. Кондрик, Г.П. Ковтун, О.П. Щербань, Д.О. Солопіхін
Представлені аналітичні та експериментальні дослідження процесу рафінування кадмію та цинку у вакуумі із засто-
суванням гетерних фільтрів зі сплаву Zr-Fe від домішок проникнення (C, N, O). Виконанo термодинамічний аналіз від-
новних реакцій оксидів кадмію, цинку, вуглецю і нітриду цинку з матеріалом гетера зі сплаву Zr-Fe в залежності від
температури та вакуумних умов проведення процесу рафінування цих металів. Експериментально показана ефективність
застосування гетерного фільтра зі сплаву Zr (51)-Fe (49) мас.% для очищення Cd і Zn від домішок проникнення.
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