summary - university of surreyepubs.surrey.ac.uk/848442/1/10803991.pdf · the chromium thiocyanate...

160
ION EXCHM&E AND OTHER STUDIES OF SOME COMPOUNDS Off THORIUM Keith A. J. Sugars Being a Thesis presented for the Degree of Doctor of Philosophy in the University of London Inorganic Research Laboratory, Battersea College of Technology, LONDON, S .W .ll. October, 1959.

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Page 1: SUMMARY - University of Surreyepubs.surrey.ac.uk/848442/1/10803991.pdf · the chromium thiocyanate system investigated by King and Dismukes (19)* This method is also used for the

ION EXCHM&E AND OTHER STUDIES OF

SOME COMPOUNDS Off THORIUM

Keith A. J. Sugars

Being a Thesis presented for the

Degree of Doctor of Philosophy in the

U niversity of London

Inorganic Research Laboratory,

Battersea College of Technology,

LONDON, S .W .ll. October, 1959.

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S U M M A R Y

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The aim of the work described in th is th e s is has been to further

the knowledge of the behaviour of thorium in acid so lu tio n s.

In connection with th is object, a review of the liter a tu re showed

that there was some disagreement, p articu lar ly as to the behaviour of

thorium in n itr ic acid , and in addition, there was l i t t l e evidence con­

cerning the reactions of thorium in phosphoric acid media.

The various sytems were in vestigated by means of ion exchange

methods and the p o sitio n has been c la r if ie d to a large extent with

respect to the types of species present. Structures for the complex

ions present are ten ta tiv e ly proposed and p ossib le explanations of the

observed phenomena are discussed.

During the course of the work i t was necessary to design methods

for the preparation of pure solu tions of thorium perchlorate and thorium

phosphate. In addition no accurate method was available for the quantita­

t iv e determination of thorium in the presence of phosphate or for sulphate

in the presence of thorium. Two methods of separation have been designed

to enable these determinations to be carried out accurately.

The phenomenon of the co -p rec ip ita tion of thorium with barium su l­

phate which was encountered in the course of a survey of a n a ly tica l methods

was found to be worthy of fu l le r in v estig a tio n , p articu lar ly as the pub­

lish ed information was scanty. Studies including those u t i l iz in g X-ray

diagrams in d icate that complex formation i s not involved but a f in a l

explanation of this process has not proved to be forthcoming.

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P R E F A C E

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The work in th is th e s is was carried out in the inorganic

research laboratory of the Chemistry Department, Battersea College of

Technology, under the supervision of Dr. J. E. Salmon, to whom thanks

are due fo r h is constant advice and encouragement throughout the course

of th is work. Thanks are due to Dr. D. J. Lewis of the Crystallography

Section of the College, for advice in connection with the X-ray stu d ies.

Thanks are also due to my colleagues in the inorganic research lab orator ies.

The UcK.AoEoAo are to be thanked for a grant and for permission

to publish the work in Part I I .

Further thanks are due to Mr, G-odby, Chief Laboratory Technician,

and h is s ta f f for th eir never fa il in g co-operation.

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INDEX page no.

Reasons for undertaking the present ?rork . . . . . . . . . .......................... 8

General Introduction

Ion-Exchange, H istorica l . . . . . . . . . . ........................................ 12

Column technique ............................ 14

Batch tech n iq u e ................................................. 14

Cation exchange res in s , preparation and

properties of . . • • • ........................ 16

Anion exchange resin s , preparation and

properties of 21

Part I

Ion exchange studies of the behaviour of thorium in acid so lu tion

H isto r ica l . . . . . . . . . . . . ..................... . . . . . . . . . . . . . . . . . . . 28

Scope of the Work •» • ...... 33

Experimental . 34 -.;

Analysis .

Determination of thorium (phosphate absent)

by t itr a t io n with EoD.T.A. ............ 43

Determination of thorium (phosphate present)

spectrophotom etrioally . . . . . . . . . . . . . . . . 47

Determination of thorium (phosphate present)

by means of ion-exchange - Method I . . . , 38

Method I I . . . . 59

D iscussion of method 64

Analyses fo r other groups ............ 67

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page no.

Part I (contd .)

Results and Discussion ...............

Results - General . . . . . . . . . . ............ . . •. 68

Cation exchange . » . . . ........... 70

Anion exchange .. . . . . . . . . ............................. 71

Discussion - Cation exchange experiments .............................. 12

Anion exchange experiments ........................... • 74-

Tabular Re su its for Part I ............ 79

Part II

C oprecipitation studies of thorium and barium sulphates

H isto r ica l 104-

Scope of the Work ................................................ .. 108

X-Ray Crystallography, an Introduction • • . . • • • * « 109

Experimental

P recip ita tion procedures ................... 115

X-Ray p roced u res . ........................... 117

R esults and Discussion

P recip itation stud ies .......................... 120

X-Ray d iffra ctio n stu d ies 123

Tabular R esults fo r Part I I .......................... 129

Part I II

Summary of Conclusions ......................................................... 154-

Bibliography .............. o 158

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R E A S O N S F O R U N D E R T A K I N G -

T H E P R E S E N T WO R K

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Thorium and certa in of i t s compounds have heen the subject of

extensive in v estig a tio n s, p articu lar ly with reference to th e ir use in the

Atomic Energy Industry. However, several features of the behaviour of

the thorium ion in acid so lu tion s t i l l require elucidation .

Studies of some o f the Complex ions formed by thorium have been

carried out, generally by means of solvent extraction procedures. There

appeared to have been very l i t t l e work performed on the behaviour of the

thorium ion in acid so lu tion and, in fa c t , at the commencement of th is

work only the thorium-hydrochloric acid system had been studied in d e ta il .

During the course of th is work papers appeared dealing with the thorium-

n itr ic acid system but these T ere co n flic t in g in th e ir conclusions.

During the in v estig a tio n s carried out fo r th is work the phenomenon

of the carrier p rec ip ita tio n of thorium by barium sulphate was encountered,

and th is was f e l t to be a subject worthy of fu l le r in v estig a tio n . The

liter a tu re on the top ic appeared to be p a rticu la r ly scant and the conclu­

sions reached by e a r lie r workers were c o n flic t in g .

The objects of the present work can, therefore, be b r ie f ly summarized

under the follow ing headings

1, To attempt an elucidation of the degree of complex formation

of the thorium ion with inorganic anions in acid so lu tion s at

various concentrations and pH values.

2. "Where p o ssib le , to suggest the ion ic species formed in these

so lu tio n s.

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3# To attempt to c la r ify the s itu a tio n with regard to the

thorium -nitric acid system,

if# To attempt an elu cid ation of the carrier p recip ita tio n of

thorium by barium sulphate, e sp ec ia lly with regard to the

p o s s ib il ity o f complex formation.

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G E N E R A L I N T R O D U C T I O N

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IO N EXCHANGE

H isto r ic a l: Ion exchange was f i r s t observed about 100 years ago by

Thompson and Way (1 ,2 ) , who in vestiga ted the phenomenon from the s o i l

chemistry aspect. This was follow ed by a considerable amount of work

with natural z e o lite s and, in p articu lar , th e ir use as water softeners was

in vestigated . Later a r t i f i c ia l z e o lite s were prepared mainly fo r use as

water softeners and th is considerably widened the f ie ld o f application

(3, 4 , 5 )* A great advance was made when, in 1935, a r t i f i c ia l ion exchange

resin s were f i r s t prepared by Adams and Holmes (6 ) . At about the same

time considerable research on resin s was in it ia te d in G-ermany; the work

has been summarized by G-riessbach (7) . Subsequent development of resin s

has enabled them to be used su ccessfu lly fo r ion separations on a n a ly tica l

and in d u str ia l sca les and as a research technique, e . g . in the study of

the nature of complex ions in so lu tio n .

Use in Study of Complex Ions: As w i l l be seen la te r (page 16 ), a res in

co n s is ts of an 'inert* matrix to which are attached active groups, e . g .

SO H. Consider the case of a cation exchanger in the metal form in acid

so lu tion :-

Mm+ + mH+ + mH+ 1 .

Where the barred formulae refer to the resin phase. This reaction i s

independent of any anions present unless complexes are formed. I f A**

i s an anion, reactions such as s-

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Mm+ + nA~ ‘FiA j X+ 2 (a ).

i t* + PA~ l M ^ ] ° 2 (b).

}iQ'+ + q if [MA^]y" 2(c)

may oc^ur. The e f fe c t of these reactions w i l l be to d isp lace equation

1 to the r ig h t. The extent of the displacement w i l l be a measure of

the complex formation, A sim ilar equation may be w ritten fo r anion

exchangers.

Ion exchange was f i r s t used in the study of complexes by Geunther-

Schulze in 1922 fo r an in v estig a tio n of the complexes formed between

ch loride’ ions and b iva len t metal ions (8 ). Gustavson also used the method

in the study of ions present in chrome liquors in the leather industry

(9, 10) , but the e a r lie r in v estig a tio n s in th is f ie ld were lim ited by the

nature o f the exchangers available at the time and, in p articu lar , by

the fa c t that they were decomposed by acid s.

Since the discovery of ion exchange resins many more exchange

studies of complex systems have been made and have generally been carried

out for two main purposes

1. The study of the nature of complex ion s.

2. The development of complexing eluants fo r the separation of

d ifferen t ion s.

Most of the methods (11, 12) fo r the former purpose are applicable

only at low concentrations of the ions undergoing exchange. However,

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Salmon and co-v/orkers (13, 14) have developed a batch method which i s

su itab le fo r use with more concentrated so lu tio n s.

In the case of the la t te r object many complexing eluants have been

found and these methods are now used on an in d u str ia l sca le for the sepa­

ration of many d ifferen t io n s. Examples of th is are to be found in the

separation of thorium and protoactinium (15), and also in the separation

of the elements curium, berkelium, and californium by means of e lu tion

with c i t r ic (16) and la c t ic (17) acid s.

Experimental Techniques: There are two experimental methods of approach

to these problems s-

( i ) Column technique

( i i ) Batch technique

( i ) Column technique

This method involves e lu tin g a column of the resin on which a band

of the complex ion has been sorbed and fo llow ing the process by analysis

of the e lu a te . The method has been used fo r the study of the nature

of complex ion s, for example, in v estig a tio n of the complexes formed in

the chromium thiocyanate system in vestigated by King and Dismukes (19)*

This method i s also used for the separation of ions from columns of resin

by means of complexing e lu an ts, e . g . separation of the transuranic elements

by e lu tio n with c i t r ic and la c t ic acids ( l6 , 18, 17 ).

( i i ) Batch technique

In the batch technique known q u an tities of res in and so lu tion are

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i

allowed to reach equ ilib rium and then analysed. This method has been j

used ex ten s iv e ly by Gustavson (20, 21, 22) and Theis and Thorstensen j

(23, 24). I

According to Gustavson (21) and a lso Salmon (25), the method has j

certa in advantages over the column procedure; these are : -

(a) that smaller q u an tities of the exchanger and sm aller volumes

of so lu tion may be employed.

(b) that attainment of equilibrium may be hastened by shaking the j

exchanger with the so lu tion . j

(c) that the extent of exchange a fter a given time may be determined, i

as rapid separation of resin and so lu tion i s p ossib le by f i l t r a ­

tio n under suction . [

(d) that the resu lts of quantitative experiments are more e a s ily

in terpreted. j

Schubert and co-workers (26, 27, 28) used very small rad io -active

tracer quantities of m etallic elements for the study of such systems as

the a lkaline earth complexes with organic acid s.

The batch method developed by Salmon (13) has been used for the [

study of phosphate complexes by Jameson and Salmon (14, 29). k sim ilar

method has been used by L ister and McDonald fo r the study of zirconium |

complexes (30) . I

Throughout the course of th is work the batch method has been used

for the study of the complex systems and the column technique fo r prepara­

t iv e and a n a ly tica l work.

During the past twenty years the development of such methods has

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been rapid and ion exchange techniques are availab le fo r many purposes

both in industry and in the laboratory.

Cation Exchange Resins

Ion exchange res in s may, fo r many purposes, be regarded as in ­

solub le. The active exchange centres of ca tio n ic resins are acid ic or

phenolic groups, and the resin matrix c o n s is ts of an in er t polymer

network attached to which are the io n isa b le groups. The polymer network

must be unaffected by so lu tion s of strong acid s, a lk a lis and common

oxid ising or reducing agents and i t must also be completely in so lu b le

in water or any other medium in which i t i s to be used. The polymers

generally employed for resin s are styrene cross-lin k ed with d iv in y l-

benzene, and methacrylic acid cross-linked with divinylbenzene, both

of which are su itab ly in ert and in so lu b le .

Various ion isab le groups have been used and in the case of cation

exchangers using ac id ic groups the most commonly used are :-

sulphonic -S0?Hj

carboxylic -COOH

phenolic -OH

phosphonic acid -P0,Ho

phosphonous acid

The exchange properties of the r e s in w i l l , to a large extent, depend upon

the ion isab le group chosen. These groups may be attached to one of the

monomers as in the case of methacrylic acid, or may be introduced a fter

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the polymer has been prepared.

Resins are prepared by suspension polym erisation (31, 32),

which i s e s se n t ia lly sim ilar to a bulk polym erisation in ?7hich the

monomers are dispersed in to d iscrete g lobules, separated and maintained

at constant temperature by an aqueous so lu tion (33)• To prevent aggre­

gation o f the monomer droplets a suspension s ta b il is e r , such as poly­

v in y l alcohol or starch, i s used. The d istr ib u tio n of p a r tic le s iz e s

in the product depends (among other fa c to rs) on the degree of mechanical

a g ita tio n , the nature of the suspension s ta b il is e r and the v is c o s ity o f

the so lu tion (34)* With polymethacrylic acid re s in s , the required

ion isab le groups are already present, but with polystyrene res in s , they

have to be introduced. The sulphonic acid groups can be introduced

by means of the usual sulphonating agents, one group being introduced

fo r each aromatic nucleus. Figures 1 and 2 show the formulae and pre­

paration of these two types of res in .

The exchange properties of a resin depend to a large exten t on the

ion isab le groups present but a lso on the basic polymer. A resin when

placed in a solvent sw ells , and the amount o f sw elling i s dependent on

the degree o f cross-lin k in g , a resin with a low degree o f cro ss-lin k in g

sw elling to a greater extent than one that i s h ighly cross-lin k ed (32).

Some idea o f the degree of cro ss-lin k in g can be obtained from an arb itrary

figure known as water regain (or weight sw e llin g ). Water regain being

defined as the amount of water sorbed by a given sample of re s in divided

by the weight of that sample. I t has been shown both th e o r e tic a lly

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and in practice (35, 36, 37, 38) that water regain i s an important factor

in exchange reaction s. In t ig h t ly cross-link ed resin s only the surface

groups can play much part in exchange reactions whereas in lo o se ly cro ss-

linked res in s , the resin i s almost part of the aqueous phase.

The resin s can be s e le c tiv e in the ions which they sorb. This

s e le c t iv ity appears both in the sorption of ions of d ifferen t io n ic charge

and also in that of ions of the same ion ic charge, but of d ifferen t

hydrated ion ic radius. This leads to the p referen tia l absorption of

ions of higher ion ic charge from d ilu te so lu tion s, but of ions of low ion ic

charge from concentrated so lu tion , w h ilst fo r ions of the same io n ic charge

those of lov/er hydrated ion ic radius are sorbed p re feren tia lly . For

resin s with a low degree of cross-lin k in g the s e le c t iv i t y w ill be le s s

than fo r those with a high degree of cro ss-lin k in g .

In general, cation exchange resin s can be divided in to two main

types, strongly acid ic or weakly acidic according to the io n isa b le group,

sulphonic acid groups being ty p ica l of the strongly acid ic groups and

carboxylic groups of the weakly acid ic re s in s . The early synthetic

resin s were polyfunctional types with two or more d ifferen t groups, such

as phenol and sulphonic acid, but these are now le s s common.

A strongly acid ic res in i s ion ised under almost a l l conditions and

the theoratlcsal capacity, i . e . the to ta l capacity due to a l l the io n isa b le

hydrogen groups, can be obtained over a wide range of pH values (39 ).

The s a lts are stab le and excess of strong acid i s required fo r regeneration.

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FIGURE IPREPARATION OF A POLYSTYRENE C A T IO N -E X C H A N G E RESIN

CH ! CH

STYRENEI----------

-C H -C H

-C H -C H -

SO

CH=CH2

v NCH=CH DIVINYL BENZENE ‘ \

SUSPENSIONPOLYMERIZATION

- c h 2- c h - c h 2 -

CROSS LINKED POLYSTYRENE

SULPHONATIONICHg- CH - CHa - CH - CH2 - CH* CH

S03HH

- c h 2- c h - c h 2-

SU IPH O N ATED CROSS-LINKED POLYSTYRENE

CSTRONGLY ACIDIC RESIN)

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FIGURE 2THE PREPARATION OF A P O L Y M E T H A C R Y L IC

CATION* EXCHANGE RESIN

c h 3

Ic*c h2

COOH METHACRYLIC

ACIO

SUSPENSIONPOLYMERIZATION

1CH3 CH3 CH3

C — CH£- C — CH2— c CHg— C H — CH —

COOH COOH COOHI

—CH -C H £—

CROSS- LINKED POLYMETHACRYLIC ACID

ACID

CH - CH

DIVINYL BENZENE

(WEAKLY ACID RESIN)

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Both the exchange o f hydrogen ions and metal ions and the reverse reaction

proceed rapidly to completion provided there i s an excess of exchanging

ion present.

Weakly acid ic res in s behave quite d ifferen tly , the capacity i s very

Ijw in acid so lu tions and the th eoretica l capacity can only be obtained

in a lk a lin e so lu tio n s. The s a lts hydrolyse on washing with water and the

resin s are read ily regenerated. The rate of exchange in the preparation

of s a lt from free acid, i s very slow, but regeneration proceeds rapidly

and only a s lig h t excess of acid i s required . These d ifferen ces in be­

haviour of strongly and weakly acidic resin s can be attributed to

d ifferen ces in the extent of d isso c ia tio n . The r a te s of exchange are

thought to be dependent on two d ifferen t processes (40) ,

The resin may be regarded, for most reaction s, as an in so lu b le

acid or s a l t . The general exchange reaction i s given by the equation

where R represents the res in and M the metal ion . The reaction i s

stoich iom etric and rev ers ib le . I t fo llow s the usual ru les , such as the

law of mass action and, i f one of the ions i s removed from the system,

fo r example, by complex formation, the reaction w il l tend to go to com­

p letio n in one d irection . Except with ions that are too large to

penetrate the polymer network, the to ta l capacity o f the r e s in i s the

same for a l l io n s.

xR-H+ + M* 5= * R -M + xH+ x

The same general considerations apply to anion exchange r es in s

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as to cation exchange re s in s , Anion exchange resin s are b asic in

character and the ion isab le groups used are, generally, quarternary

ammonium, or a lip h atic or aromatic amine groups, the quarternary ammonium

groups giving strongly basic re s in s , the others being weakly b a sic .

The anion exchange resin s are prepared in a sim ilar manner to that

mentioned previously (for cation exchangers) F ig, 3, showing the

formulae and preparation of these types (4-1, 42), Other methods are

available fo r the preparation of anion exchange resin s (43, 44, 45) •

A strongly basic anion exchanger has a capacity which i s independent

of the pH of the so lu tion . These resin s can be used for the uptake

of strong or weak acid ic compounds, e . g . amino acids (46), and can a lso

take up certa in metal ions q u an tita tive ly from so lu tion s by formation of

an anionic complex, e . g . FeCl^ from concentrated hydrochloric acid .

On the other hand the capacity of weakly acid ic resin s depends to a

marked degree on the pH of the so lu tio n . At low pH these exchangers

are h ighly ion ised whereas at high pH values they are unionised and

in er t (47)* The s a lt s of strongly b a s ic resins are sta b le whereas

those of weakly b asic res in s hydrolyse on washing. To regenerate a

strongly basic res in a large excess of strong base i s required and the

rates of exchange are normally rapid. In the case of anion exchangers

of weakly basic type they are read ily regenerated with sodium carbonate

and unless ion ised the r a te s of exchange are slow.

Factors a ffectin g the Exchange R eaction; These factors can be divided

in to t?/o groups, (a) those variables prim arily connected with the re s in

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FIGURE 3

PREPARATION OF ANION EXCHANGE R E SIN S FR O MCROSS-LINKED POLYSTYRENE

CH— C H ,— CH — CH — . CH— CH — CH— CH 2 | 2. | 2 a

CH - C H -C H 2

CROSS LINKED POLYSTYRENE

CHLOR OM E TH YLA TION

C H — CHP - CH — CH

C H -C H -C H 2

CHLOROMETHYLATED CROSS-LINKED POLYSTYRENE

I--------------------t r im e t h l a m in e

+- c h - c h 2

DIMETHYLAMINEi- C R -C H ,

CHeNt (CH3) 3 cL STRONGLY BASIC RESIN

‘CHN(CHVa WEAKLY BASIC RESIN

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i t s e l f , i . e . :

Type of ion isab le group,

Degree of cross-lin k in g ,

Size o f resin bead,

and (b) the conditions under which the exchange reaction can be carried

out :

Strength o f acid,

Temperature,

Time of contact (for batch work),

' Rate of flow (fo r column work).

A strongly acid ic ca tion ic resin , ZeoKarb 225> and a strongly b asic

exchanger, DeAcidite FF, were employed throughout the work

described. The reasons fo r th is choice can be summarized as follow s ;

Strongly acid ic and strongly basic res in s are :

( i ) Ionised under almost a l l conditions of pH and hence the

th eo retica l capacity can be obtained over a wide range of pH

values.

( ii)T h e ir s a lts are sta b le .

( ii i)r h e lr exchange i s rapid and proceeds to completion.

Weakly acid and weakly basic res in s do not possess a l l of the above

ch a ra cter istics and i t was f e l t that no advantage was to be obtained

from th eir use.

The degree of cross-lin k in g i s important in th a t, with a strongly

acid resin the sw elling (in \?ater) increases rapidly as the proportion

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of clivinylbenzene i s deoreased. Furthermore, the resin volume de­

creases as the strength of the acid eluant i s increased and th is e ffe c t

i s greatest in lov/ cross-link ed res in s . For batch experiments, the

degree of sw elling i s r e la t iv e ly unimportant, but fo r column work a small

change in volume i s desirable and a h ighly cross-lin k ed res in would seem

more su ita b le . Unfortunately, the degree of cro ss-lin k in g a lso has an

e ffe c t on the rate of exchange which i s u su ally dependent on one c f two

factors (4-1 )

(1) Film d iffu sion , i . e . d iffu sion across the film immediately

adjacent to the resin bead.

(2) P artic le d iffu sio n , i . e . d iffu sio n w ithin the resin bead i t s e l f .

For most processes film d iffu sio n i s the rate determining fa cto r and

p a rtic le d iffu sion need only be considered when veiy large ions are

involved or a very highly cross-lin k ed resin matrix i s being used. In

practice a compromise i s u su ally necessary and resin s with about ten per

cent divinylbenzene cross-lin k in g are most su ita b le . However, res in s

of d ifferen t degrees of cross-lin k in g were used in some experiments to

see whether there was any e f f e c t on the exchange reaction .

Again for batch experiments, the s iz e of the res in beads i s r e la ­

t iv e ly unimportant but i t i s preferable to maintain the same s iz e bead

for any one ser ie s of experiments.

The strength of the acid eluant can a ffe c t the rate of exchange.

With a strongly acid ic or strongly basic re s in , i f the concentration

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of exchanging ions in so lution i s low, the rate con tro llin g process

i s largely film d iffu sion , but as the concentration i s increased,

the d iffu sion of ions w ithin the p a r tic le becomes more important

(48).

An increase in temperature w il l increase the r a te of rea ctio n

(in most cases) but should not a ffe c t the equilibrium s ta te .

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P A R T I

ION EXCHANGE STUDIES OF THE BEHAVIOUR OP THORIUM

IN ACID SOLUTION

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HISTORICAL

SURVEY OF THORIUM COMPLEXES WITH INORGANIC ANIONS

Thorium shows a strong tendency to form complexes with anions.

Evidence e x is ts fo r , among others, complexes with flu orid e (4-9* 50* 51)*

n itra te (4-9* 50), chloride (4-9* 50, 52), chlorate (4-9)* sulphate (50),

sulphite (56, 57)* carbonate (53* 54-, 55)* and many organic anions. Com­

plexes with phosphate (50) have also been suggested. Some of these complexes

are l i s t e d below :-

Anion Suggested Complexes

e“ . ThE5+, ThF0++, TKF A

Cl" ThCl3+, ThCl2++, ThCl*

n o "5 E i(N03 ) 3+, Ih(N03 ) 2++.

CIO “ 5

Th(C103 ) 3+.

HSO " 4- Th(S04 )++.1^■4-s

Th(HP0,)3+, Th(HgP0. ) 2+

The equilibrium constants for the formation of these complexes

have been determined and in the m ajority of cases they have been found by

means of the solvent extraction method with thenoyltrifluoroacetone as

chelating agent in the presence of high concentrations of perchlorate io n s.

Another symptom of the ready formation of complexes i s the tendency

of thorium to form double s a lt s . A lkali metal double s a lt s are formed

with a l l the common anions, and double s a lt s with other types o f cation are

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known.

Ion Exchange in th e Study of Thorium Complexes

As a resu lt of the combination of high charge and low hydrolysis thoriur

i s p articu larly read ily absorbable on cation exchangers (58), and owing to

i t s readiness to form complexes, as w il l be seen la te r , i t can a lso o ften I

be absorbed by anion exchangers.

An example o f the former tendency i s to be found in the separation

of the thorium isotope UX- (Th ) from i t s parent uranium (59) • B r ie fly ,

the method i s to pass a so lu tion of uranyl n itra te through a bed of cation

exchange res in , both the uranium and thorium are retained . The uranium

i s eluted with d ilu te sulphuric acid and the absorbed thorium isotop es are

then washed out with oxalic acid .

In recent years a considerable amount of work has been carried out

on the complex chemistry of thorium, but, as y e t , i t has not been f u lly

elucidated . In 195& Kraus, Moore and Nelson stud ied the behaviour of

thorium in hydrochloric acid so lu tion by means o f anion exchangers and

found no evidence of complex formation (6 0 ). They a lso studied the be- j

haviour of thorium in lithium chloride so lu tion s and suggested that negative- j

i

ly charged complexes may be formed but the data were not s u ff ic ie n t to j

esta b lish th is unambiguously. The doubt concerning the formation of

anionic chloro complexes was confirmed by Hyde who stated that thorium

forms no negatively charged complexes in hydrochloric acid o f any concen­

tra tio n (6l ) . j

Schulz and Herak ( 63) have also studied, using the method of Kraus

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and Nelson ( 64) , the ca tion ic complexes formed by thorium in hydrochloric

acid of concentrations between 0.1N and 5N. These authors concluded that

there may be a prevalence of the complex ThCX *"1"* The conclusions

arrived at may be open to some doubt in that a thorium n itra te so lu tion

was used for these experiments and, as w i l l be seen la te r , the presence

of even small amounts of n itra te ion has an e f fe c t on the behaviour of

thorium in hydrochloric acid so lu tion .

The above authors a lso studied the complex formation of thorium

in , amongst others, n itr ic acid and sodium n itra te media. The complex,

Th(N0^)2++ was suggested as being the most prevalent.

Danon (65) , in 1958, using an anion exchanger, found that the metal

i s sorbed from a so lu tion of thorium in n itr ic acid and that th is sorption

i s greatest when the n itr ic acid concentration i s 7M and suggests that

n egatively charged complexes of thorium are being formed or are dominant

at 7M n itr ic acid . In another paper (66) , the same author found that

thorium i s retained on an anion exchanger a fter passage of a so lu tion of

thorium in 5M n itr ic acid and i s read ily elu ted with 2.6M hydrochloric acid .

On the other hand Hyde ( 6l ) ( and also Katz and Seaborg ( 62) ) , s ta te s that

thorium forms no n egative ly charged complexes in n itr ic acid of any con­

centration, and further th at passage of a thorium containing solution

through a column of an anion exchange r e s in w i l l separate thorium clean ly

from any elements which do form absorbable negative ion s. Hyde further

suggests th at, owing to the ready absorption of thorium on cation exchange

resins and the fa c t that i t i s not desorbed at any appreciable rate with

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any concentration of n itr ic or hydrochloric acid , a simple way to separate

thorium from most elements i s to absorb i t on a cation exchange column.

Then, by exhaustively washing with 6M hydrochloric acid or n itr ic acid,

the simple monovalent and d ivalent ions pass through the column immediately.

The rare earth elements require a considerable volume o f acid fo r th e ir

complete removal but the e lu tio n of thorium does not begin u n t il long a fter

the rare earths have gone.

I t i s in terestin g to note that on a consideration of io n ic radix

alone one would expect the tendency to form complexes to be greater with

chloride ions than with n itra te io n s. Hindman (67), however, has shown

that the reversal o f the order can be expected due to the structure of the

n itra te ion and i t s resu ltin g high p o la r isa b ility . Of elements previously

studied only Neodymium ( i l l ) , Praesodymium ( i l l ) , Samarium ( i l l ) and

Europium ( i l l ) , ( 67) and the transuranic elem ents, such as Plutonium ( i l l ) ,

Plutonium (IV) and Americium ( i l l ) , (68) have le s s tendency to complex

formation with chloride than with n itra te .

Schulz and Herak ( 63) a lso worked on the thorium-sulphuric acid

system and have suggested the t r ip le charged complex Th(HS0^)+++, but

the method i s again open to objection in that n itra te ions were present

from the thorium n itra te so lu tion used.

A large amount o f work has been performed in the study of metal

complexes and in many cases the s itu a tio n has been fu lly e lu cid ated . A

consideration of the foregoing shows that th is i s not so with thorium,

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and in fa c t there are s t i l l a number of points to be c la r if ie d . I t can

be seen that in the case of thorium in chloride so lu tion s there i s good

agreement as to the non-formation of anionic complexes but in the case

of n itra te so lu tion s, there i s some disagreement as to whether or not

th is i s the case.

In sulphate so lu tion there i s very l i t t l e anion exchange evidence

of complex formation availab le and further work appears necessary. No

work dealing with thorium complexes in phosphoric acid by means of ion

exchange could be found in the l ite r a tu r e .

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SCOPE OF THE WORK

From the previous sec tio n i t has been seen th a t fu r th e r work was

necessary on the s ta te of the thorium ion in n i t r a t e and sulphate so lu ­

t io n s . A ccordingly, by means of ion exchange, experiments were c a r r ie d

out to t r y and achieve th i s end. Both c a tio n exchange and anion exchange

r e s in s were used. An attem pt has been made to e lu c id a te the degree of

complex form ation of thorium in h y d ro ch lo ric , n i t r i c , su lphuric and

phosphoric ac id so lu tio n s . Some experim ents have a lso been performed*

in arsen ic ac id media.

I t proved necessary during the course of the work to dev ia te a

l i t t l e from the main o b jec tiv e in o rder to f in d new a n a ly t ic a l methods

fo r the determ ina tion of thorium in th e presence of phosphate, and of

sulphate in the presence of thorium .

As a r e s u l t of the experim ents conducted the a n a ly t ic a l d i f f i ­

c u l t ie s have been overcome and suggestions have been made as to the

nature of complex form ation and in some cases d e f in ite com positions

have been assigned to the complexes.

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EXPERIMSNTAL

(1) M ateria ls

Cation Exchange R esins: The resin used throughout the work fo r the

cation exchange experiments was ZeoKarb 225, a strongly acid polystyrene

resin . This was supplied i n i t i a l l y in the hydrogen form, and bulk prepara­

tions were carried out in a g la ss column of conventional design, approxi­

mately 10 in s , high and j ” in diameter, f i t t e d with a grade 2 sin tered

glass disc sealed in to the base and capable of holding about 25gr.of re s in .

As obtained com m ercially the r e s in contained app rec iab le q u a n ti t ie s of iro n

and th is was removed by running through the column an excess (c a . 200 m l.)

of 2N hydroch lo ric ac id , a t a flow ra te of about 2 ml, per m inute, follow ed

by deion ised w a te r ,u n t i l the washings were f re e o f ch lo rid e io n s .

Thorium form R esin : A fte r washing w ith w ater the re s in was t r e a te d

w ith an excess o f approxim ately N/lO thorium n i t r a t e o r thorium c h lo rid e

so lu tio n . The r e s in was again washed w ith w ater u n t i l the washings con­

ta in ed no tra c e of thorium (as in d ic a te d by the lack of a p r e c ip i ta te w ith

ammonium hydroxide). I t was then f i l t e r e d o ff and allow ed to dry in a i r .

The dry re s in s were then s ieved to a uniform s iz e .

Anion Exchange R esins; In th is instance the res in used was

DeAcidite FF, a strongly basic polystyrene r es in , the active s i t e s being

quarternary ammonium groups. This type was obtained i n i t i a l l y in the

chloride form, and was treated in a column, as above, with 2N hydrochloric

acid to remove im purities. The resin was washed with water u n til the

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washings gave no trace of the chloride ion on treatment with n itr ic acid

and s ilv e r n itra te . The resin was then a ir dried.

Various forms of the re s in were required and these were prepared

by taking the chloride form and passing an excess of the so lu tion s ind icated

below, washing with water u n t il the washings contained no trace of the

anion under consideration, and fo llow ing th is by a ir drying.

Resin form required Solution used

CIO* 2N HC10,4 4

S°” 2N Na2S0^

NO* 2N m o ,3 3

P0^! * 2N NaH2P0^ + 2N Na2HP0 *

* The so lu tion used contained one volume of Na2HP0 containing 284 g . / l i t r e

and s ix volumes of NaHgPO (312 g n /ll'tre ); th is gave a so lu tion o f aa.pH 5*

Water: A ll water used was f i r s t d i s t i l l e d in g lass and then passed,

immediately before use, through a column o f biodem inrolit to complete the

deionisation process.

Reagents: A ll reagents were of a n a ly tica l grade.

Solutions of thorium perchlorate and thorium phosphate.

Thorium perchlorate - This m aterial was not obtainable commercially and was

prepared by repeatedly passing 2N perchloric acid down a column of thorium

form ZeoKarb 225* The column used was about 10 in s . high and \ in . in

diameter and held about 25 g . of resin* The res in was washed and r e -

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genera ted (to the thorium form) between each passage of so lu tion . The

r e su lt was a so lu tion of thorium in perchloric acid . Upon evaporation

white cry sta ls were obtained which, when analysed, had formula Th(ClO^)^*

Thorium phosphate - A so lu tion of thorium (ca. N/lO) in phosphoric acid

(10M) was prepared by adding an accurately weighed quantity of about 7*1 S •

of thorium carbonate to 133 c .c s . o f concentrated phosphoric acid . The

solution was then made 10M' in phosphoric acid by d ilu tion with water, and

the thorium strength was found by ca lcu la tion . I t proved im possible to

obtain cr y s ta llin e thorium phosphate - the above so lu tion gave on d ilu tion

with water a white gelatinous p rec ip ita te .

(2) Apparatus

A ll g lass apparatus was cleaned with dichrornate-sulphuric acid

mixture and washed twice with tap water and then twice with de-ion ised

water. Flasks used in batch experiments were dried in an oven at 110°C.

The rubber bungs used were b o iled in d ilu te sodium carbonate so lu tion ,

then in d ilu te hydrochloric acid and f in a l ly washed severa l times with

d is t i l le d water.

(3) Batch Ion Exchange Experiments

Discussion of Method: The general technique employed was to weigh

out a given quantity of the appropriate re s in , and to leave th is immersed

for seven days in a measured volume of the required so lu tion . Seven days

being the time found necessary fo r equilibrium to be achieved; however,

in some cases th is procedure had to be varied due to p rec ip ita tio n . A fter

standing, the so lu tion was then f i l t e r e d o ff and an a liquot taken and

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analysed, Occasionally i t was necessary to analyse the species retained

on the resin , e .g . when phosphate ions were present.

In order to obtain the required accuracy in weighing, i t was

necessary to dry the resin , th is drying being always carried out at room

temperature. Later, in connection with certa in anion exchange stu d ies,

experiments were performed on the drying of the r e s in s . These w il l be

discussed la te r in the section dealing with r e su lts .

In the majority of the experiments the r e s in used was fu lly loaded,

that i s , a l l the replaceable hydrogen ions had been replaced by thorium

ions, but occasionally i t proved inconvenient to achieve f u l l loading.

Experiments were therefore carried out in an e ffo r t to ascerta in whether

incomplete loading had any e f fe c t on the f in a l r e s u lts , and in fa c t i t was

shown th at, w ithin l im its , the degree of loading was not important.

I t was necessary to a g ita te the resin and so lu tion to prevent the)

build up of concentration in the v ic in ity of the beads. When beads of

f in e mesh s iz e s were used, the l ig h t beads tended to f lo a t at f i r s t and

to s tick to the sid es of the v e s se l ju st above the surface of the liq u id

unless the f la sk was shaken. An occasional gen tle sw irl was found adequate

to over come both of these d i f f i c u l t ie s .

The dry resins were sieved to a uniform mesh s iz e . A variety of

resins were used and the choice of mesh s iz e s varied, but th is was found

to be of l i t t l e importance.

Cation Exchange Experiments: Exactly 0.500 g. • of the metal form

of the resin were weighed out and placed in a 150 ml. con ica l f la sk , 50 ml.

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of acid of the appropriate strength were then added from a p ip ette and the

fla sk sealed with a rubber bung. I t was then se t aside fo r seven days

and the contents sw irled occasionally . Often i t was found to be more con­

venient to weigh out the resin beforehand in to small ig n it io n tubes and to

transfer i t la te r to the conical f la s k s . At the end of the required time

of contact, the acid was f i l t e r e d o ff in to another f la sk , and a 25 ml,

aliquot extracted with a p ip ette and analysed for the metal.

A d ifferen t procedure had to be adopted in some of the experiments

with phosphoric and arsenic acids owing to the fa c t that, i f the fla sk s were

set aside fo r seven days, p rec ip ita tio n occurred, presumably of the metal

phosphates and arsenates. This d if f ic u lty was overcome by placing the

f la sk containing the resin and so lu tion on a mechanical shaker fo r a time

consistent with the non-formation of a p rec ip ita te . This time was fotlhd

by experiment and was generally about three hours.

Since, at the time, there was no re lia b le method availab le fo r

the determination of thorium in the presence of phosphate or arsenate,

the so lu tion could not be analysed. In th is case the resin was transferred

to a small g lass column, and washed rapid ly at f i r s t and then more slow ly

with d i s t i l l e d water u n t i l the washings contained no d etectab le trace o f

phosphate ion (about one l i t r e o f water was required). F in a lly the thorium

was removed with about 150 ml. of 2N n itr ic acid . The eluate was evaporated

down to about 25 ml. and analysed fo r m etal. A ltern atively , the oluato

was made up (in a graduated f la sk ) to 500 ml. with d i s t i l l e d water, and an

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aliquot taken and analysed fo r metal. The percentage o f metal which

had been removed from the resin by the phosphoric or arsenic acid was

then obtained by d ifferen ce . The experiments were carried out at roomz+ «

temperature, 20° ( - 3 )*

Anion Exchange Experiments: In these experiments 4-0 ml. of acid

were used of a m olarity such that when 10 ml. of M/lO thorium so lu tion

were added, the m olarity became that which was required, fo r example,

40 ml. of 10M acid ?/ere placed, by means of a b urette, in the con ica l f la sk

and 10 ml. of the appropriate Wl/l0 thorium so lu tion were added. The f in a l

resu lt was, therefore, 50 ml. of a so lu tion 8M in acid and M/50 in thorium.

In the experiments with phosphoric and perchloric acids the procedure wasv ■

varied s l ig h t ly owing to the fa c t that the thorium phosphate and thorium

perchlorate were already in acid so lu tion . E sse n tia lly the procedure

was to p ip ette 10 ml. of these so lu tion s in to the f la sk s and then to add

phosphoric or perch loric acid of the appropriate strength in order to give

the required f in a l concentration.

In a l l cases, the o v era ll thorium concentration was N/50 and the

acid concentration ranged, where p o ss ib le , from 1-10M, Exactly 1.000 g .

of resin were then placed in the f la sk s , and the f la sk s were sea led with

rubber bungs and set aside as before. The number of ion ic species was

kept at a minimum by using the corresponding form of the r e s in , acid solu­

tion and thorium so lu tion , fo r example, chloride form res in , hydrochloric

acid and thorium chloride so lu tio n . A fter the required time o f contact

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the resin was f i l t e r e d o ff and an aliquot of the so lu tion taken and

analysed fo r thorium,, From th is i t was p ossib le to fin d the amount of

anionic thorium sorbed by the r e s in .

Cation Exchangers:

(a) Metal Capacity - Exactly 0,500 g , of the metal form of the

resin , prepared as previously described, were taken and placed in a small

column with a sin tered g lass base. The resin was then elu ted with an excess

(ca, 150 m l,) of 2N hydrochloric acid . The amount of thorium in the eluate

was determined and hence the capacity in m illi-eq u iv a len ts per dry gramme

could be found.

(b) Hydrogen Capacity - The hydrogen capacity was determined d irec t­

ly on the sample used fo r metal capacity determination, by washing with water

u n til the washings were free of chloride ions and then e lu tin g with approxi­

mately 2M sodium chloride; th is gave sodium form res in and hydrochloric

acid. The acid was t it r a te d with standard a lk a li and hence the hydrogen

capacity of the r e s in was known. As a check a second method was employed

in which 0.500 g • of re s in in the hydrogen form were placed in a f la sk

containing excess sodium sulphate and water, phenolphthalein ind icator

was added and the sulphuric acid lib era ted was t itr a te d with standard

a lk a li,

The resin s were prepared as previously described in batches of

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about 25 gm* Two 1,000 g • samples of each of these batches were

taken and placed in a small oolumn, these were then eluted with the

appropriate acid , foremmple, in the case of chloride form resin n itr ic

acid was used, and the e fflu en t was analysed by the usual standard

methods. This enabled values for the capacity of the resin to be

ca lcu lated .

Water Regain: (or Weight Sw elling)

This was determined by a centrifuge method based on that of

Pepper, Reichenberg and Hale (84)*

Two small tubes w ith sin tered g la ss bases (porosity grade 2)

were dried in an oven at 110°C and weighed. Approximately gm, o f wet

resin , hydrogen form in the case o f cation exchangers, and chloride form

in the case of anion exchangers, were placed in the tubes together with

a very small amount of surface active agent, to a s s is t drainage# The

tubes were then sealed with a rubber cap and centrifuged fo r one hour

at 2000 revolutions per minute. Two small holes were blown in the

tube near the cap in order to allow the in t e r s t i t i a l water to drain from

the tube unhindered w h ilst the tube was centrifuged . The tubes and

resin were weighed and then dried in an oven fo r 24 hours at llO°C for

cation exchangers and 90° fo r anion exchangers, cooled in a vacuum d e s s i-

cator over magnesium perchlorate, and again weighed. The tubes were

then emptied and immersed in water containing a surface a ctive agent,

removed, centrifuged fo r ten minutes and weighed.

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- 42-

The water regain can be calcu lated from the equation.

[/Wet weight - (Wet weight x 0 .03 )J - Dry weight

Dry weight

The correction to the wet weight has been found necessary by experiment

in order to account fo r the remaining in te r s t i t ia l , water a fter cen tr i­

fuging. ,

(4) Analysis

The a n a ly tica l methods employed were those indicated in the

follow ing sectio n .

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ANALYSIS

Thorium

In the absence of phosphate and a rsen a te thorium has been d e te r­

mined throughout the work by one or o th er o f two methods. In essence

the methods are the same, only d if f e r in g in the in d ic a to r used.

( i ) The f i r s t method ( 69, 70) made use o f the indicator pyroca-

tech ol v io le t , in a fashion sim ilar to that of Suk and Malat (70), and

b a sica lly con sisted of the t itr a t io n of the so lu tion s containing thorium

with ethylenediam inetetraacetic acid at a pH of 2 .5 - 3*5 or* 1 ,8 - 2 .2

depending on -the age of the in d icator so lu tion .

The so lu tion to be t itr a te d (containing not more than 10 mg. of

thorium) was adjusted to pH 1 ,8 by means of n itr ic acid or ammonia and

the ind icator creso l red which changes colour from red to yellow at that

point. The pyrocatechol v io le t was added to the so lu tion and the thorium

t itra ted with EDTA, the end point being when the colour changed from red

to yellow .

According to Suk and Malat the most favourable pH fo r the t it r a t io n

was 2.5 - 3«3« However, during the course of th is work considerable

d iff ic u lty was experienced at times in obtaining a good end point at

th is pH. Upon in v estig a tio n i t was found that with fresh ly prepared

indicator the b est pH v/as that recommended by the authors but a fter i t

had stood for several days a pH of 1 .8 - 2 .2 fo r the so lu tion to be

t itr a ted gave a sharper end p o in t. The authors suggested that the ind icator

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- 44-

solution was stab le in d e fin ite ly but the present observations are not in

agreement with th is .

The method v as found to be sa tis fa c to ry in the presence of a l l the

anions encountered except sulphate, phosphate, and arsenate, the phos­

phate causing the greatest in terferen ce .

The method was tested by using so lu tion s containing known amounts

of thorium as estim ated by the oxalate p rec ip ita tio n procedure (7l ) .

The re su lts obtained are summarized in Table 1 below,

( i i ) Later a second method was used, th is method being sim ilar

to that above except that the in d icator used was Xylenol Orange and was

f i r s t suggested by Korbl and P r ib il (7 2 ), The same pH was suggested for

the t itr a t io n and the same considerations as above apply with regard to

ageing of the in d icator so lu tion .

This second method was preferred fo r two main reasons, namely,

i t s sharper end point and i t s a b il i ty to give sa tis fa c to ry re su lts

in the presence o f sulphate io n s. I t was, however, unreliab le in the

presence of phosphate and arsenate. As before, the method was checked

against the standard oxalate p rec ip ita tio n procedure (71), the resu lts

of which are summarized below in Table 2,

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TABLE 1,

Determin a tio n o f thorium using EoDoToA. w ith pyrooateohol v io le t in d ic a to r

Thorium taken g.

Thorium founds .

D ifferencemg.

0,0521 0.0522 0.1

0.0492 0.0495 0.3

0.0406 0.0408 0.2

0.0324 0.0324 0.0

0.0324 0.0323 0.3l

0.0218 0.0220 0 .2

0.0139 0.0143 0 .4

0.0139 0.0142 0 .3

0.0054 0.0055 0.1

0.0048 0.0052 0.2

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TABLE 2.

Determination of thorium using E«,D,TeA0

with xylenol orange indicator

Thorium taken g.

Thorium found g.

D ifferencemg.

0,0492 0.0493 0.1

0.0406 0.0405 0.1

0.0324 0.0324 0.0

0,0324 0.0325 0.1

0,0286 0.0284 0.2

0.0218 0.0218 0.0

0.0185 0.0187 0.2

0,0185 0.0186 0.1

0.0121 0.0121 0,0

0.0121 0.0120 0.1 .

Various other volumetric (73* 74* 75)* gravimetric (76, 77), and

speotrophotometric procedures (78, 79* 8o) have appeared in the liter a tu re

"but these too are subject to in terference in the- presence of phosphate, and,

since the methods above proved sa tis fa c to ry , i t was not thought l ik e ly to

be p rofitab le to in v estig a te them further.

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Many attem pts were made to f in d an accu ra te method f o r the determ ina­

tio n of thorium in the presence of phosphate. Most of these were q u ite

u nsuccessfu l; however, th re e methods have been found, one of which i s an

ad ap ta tio n of a spectrophotom etric method and i s accu ra te to about 3 P©r

cent, the o th e rs are new ion exchange methods th a t f a l l w ell w ith in the

l im its of accuracy norm ally req u ired . One of the methods i s s a t is fa c to ry

in the presence of very la rg e excesses of phosphate,

Spectrophotometric Method: This method has been adapted from the method

due to Clinch (7 8 ). The procedure adopted was that recommended by Clinch

and by p lo ttin g a ser ies o f ca lib ra tio n curves fo r so lu tion s with various

known phosphate contents and carefu l in terpretation o f r e su lts , i t was

found p ossib le to determine to £ 3 per cent the thorium content of a so lu tion

containing phosphate. The method r e l ie s on the red colour formed by thorium

(at high d ilu tio n ) with l-(o-arsonophenylazo)-2-naphthol-3 :6-disulphonic

acid (APANS), the in te n s ity of the colour being compared, spectrophoto-

m etrically , with a blank so lu tio n . Aqueous APANS so lu tion containing

thorium shows an absorption peak at and so lu tion s containing various

amounts of thorium were compared with blanks at th is wavelength. The

resu lts obtained are given in Table 3> and these were p lo tted to give

the graph in Fig,4« From th is graph i t i s p ossib le to estim ate the amount

of thorium in an unknown so lu tion provided there are no in ter fer in g io n s.

To a so lu tio n co n ta in in g thorium (between 0 and 1*3n g .), in a 100 ml.

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- 48-

graduated f la sk , two drops of phenolphthalein were added and the so lu tion

was neutralised to a red colour with arDmonia. 10 ml* of hydrochloric

acid (1:4) were added and 15 m l. of a 1% so lu tion of APANS in water. A

blank so lu tion containing sim ilar amounts of acid and APANS was prepared.

Uach so lu tio n was made up to the mark with d is t i l l e d water and immersed in

a thermostat at 25°C for f i f t e e n minutes. The absorption at 545m(i was

then measured on a. HLlger SP600 spectrophotometer using 1 cm. c e l l s .

Standard so lu tion s o f thorium were made up and the r e su lts (Table 3)

were p lo tted to give the graph in F ig .4.

I t was found th at f lu o r id e , sulphate and phosphate ions in ter fere .

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OPT

ICAL

D

EN

SIT

Y

F I G U R E 4GRAPH OF OPTICAL D E N S ITY AGAINST

MILLIGRAMMES THORIUM AT WAVELENGTH 545 M /4 ( I N T E R F E R I N G I O N S A B S E N T )0 9 0

0-80

0-70

050

0 - 4 0

0-30

0-20

O' lO

0 O'l 0 ' 2 0-3 0 - 4 0 - 5 0 ' 6 0-7 0-8 0 ' 9 LO I I 1 2 1-3TH O R IU M (nm g)

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- 50-

Phosphate was found to in terfere and experiments were carried out

with known amounts of phosphate and thorium, a ty p ica l set of r e su lts

i s given in Table 4 and these are p lo tted in F ig .5.

Thorium taken O ptical d ensity.. mg.

0,1 0.062

0.2 0.134

0.5 0.208

0 .4 0.258

0.5 0.373

0.6 0.440

0.7 0.498

0.8 0.562

0.9 0.623

1.0 0.720

1.1 0.780

! .2 0.850

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- 51-

TABLE 4 .(A ll so lu tions contained 0.88 mg* Th)

O ptica l d en s ity o f so lu tio n s con tain ing known amounts of thoriumand phosphate

Phosphatemg.

O pt.D ensity A fte r 2 h r s .

O pt,D ensity A fte r 19 hrs

O pt.D ensity A fte r 8 days

Avg. Opt. D ensity

)R atio

0.103 0.675 0.682 0,685 0.681 0.2830.206 0.660 0.700 0.700 0.687 O.566

0.309 0.658 0.685 0.679 0.674 0.8490.412 0.670 0.695 O.690 0.685 1.132

0.515 0.671 0.695 0.690 0.685 1.4150.618 0.652 0.691 0.670 0.671 1.6980.721 0.671 0.706 0,672 0.683 1.9810.824 .0.649 0.670 0.688 0.669 2.2640.927 0.662 0.700 0.702 0.688 2.5471.03 0.670 0.678 0.704 0.684 2.8301.54 0.668 0.695 O.669 0.677 4.2452.06 0.650 0.690 0.662 O.667 5.662.58 0.662 0.695 0.690 0.682 7.073.09 0.644 0.685 0.690 0.673 8.493.60 0.651 0.700 0.700 0.684 9.904.12 0.642 0.680 0.702 0.675 11.324.63 0.639 O.67Q 0.690 0.666 12.735.15 0.641 0.692 0.660 0.664 14.157.21 0.632 0.685 0.670 0.662 19.81

10.3 0.629 0.671 0.665 0.665 28.315.45 0.639 0.655 O.660 0.650 42.520.6 0.610 0.639 0.635 0,628 56.6

25.75 0.620 0.620 0.632 0.627 70.8

30.9 0.559 0.610 0.628 0.596 84.9

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- 52-

TABLE 5.

Varying amounts of thorium and phosphate were used so as to give

the ra tio s quoted. 1 ml. of phosphate so lu tion contained 0.103 mg.

Ratio P0^/Th = 10/1

Thorium added Phosphate added Optical densitymg ml

0.176 0.70 0.180

0.352 1.41 0.292

0.528 2.12 ■0.481

0.704 2.82 0.580

0.880 3.18 0.715

1.056 4 .2 4 0.830

Ratio P0^/Th == 15/1

0.176 1.06 0.145

0.352 2.12 0.287

0.528 3.18 0.391

0.704 4 .24 0.534

0.880 5.30 0,660

1,056 6.36 0,790

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- 53-

TiJBLE 5. (Contd.)

Thorium added mg

0.176

0.352

0.528

0.704

0.880

1.056

0.176

0.352

0.528

0.704

0.880

1.056

0.176

0.352

0.528

O.704

0.880

1.056

R atio PO^/Th =

Phosphate added ml

1.41

2.82

4.23

5 .64

7.05

8.46

R atio PO^/Th

1.77

3.54

5.31

7.08

8.85

10.62

R atio PO^/Th =

2.21

4 .24

6.36

8.48

10.60

12.72

20/1

O p tica l d en sity

0.114

0.235

0.371

0.500

0.650

0.790

= 25/1

0.157

0.300

0.425

0.542

O.684

0.820

0.175

0.302

0.432

0.575

0.688

0.838

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o

oCD

CO

CO00

□cLU

^ CL3 SDC < O CO

Lli

COoCL o

CO l i i

CO

CD

Ui U-o

<CJ

ao

COCL<cr a

CJ

o ooCVi

o oincoo

ooK)co

CO

A llS N O a 1 V 0 ( ld 0

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-55-

As a r e su lt of experiments of th is type, i t was shown that the

important factor was the PO /Th ra tio and therefore a s e r ie s of experiments

was carried out using known amounts of thorium and phosphate, for example,

PO /Th : 1 0 /l , 15/1, 2 0 /l , e tc . These r e su lts are given in Table 5 an<l

p lo tted in F ig . 6 .

By means of the graph in F ig .6, i t i s p ossib le to estim ate thorium

in the presence of phosphate to an accuracy of approximately The

method used i s as fo llow s

The so lu tions to be te sted are made up in the same manner as pre~

viou sly ind icated and the reading for o p tica l density i s noted. Part of

the so lu tion i s analysed for phosphate by the usual method. Then

use i s made of the o p tica l density reading by obtaining from the graphs

values fo r the amount of thorium present from the two extreme graphs;

then, using these values, i t i s possib le to ca lcu la te two values fo r the

PO /Th r a t io . The average of these values i s token and th is i s used to

ca lcu late the amount of thorium present. An example i s given below.

A ltern atively , the o p tica l density reading i s used to give a value fo r the

amount of thorium present from the graph nearest in ra tio to the average

found.

To check the method a s e r ie s of determinations were carried out

with known amounts of thorium and phosphate. The re su lts are given in

Table 6 .

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cro

h*CO

X

COUJcr3e>

LUUJ

crLjlo

u .ocoXQ. U.

cr 0 © 0 @ @

Q. a. a. cl < < < < < a: cc qi sx □:CD CD CD CD CD cu

ajupo

coCT) COo o

A11SN3C3 IV O I ld O

0-3

0-4

0-5

Q'6

0-7

0-8

0*9

MIL

LIG

RA

MM

ES

T

HO

RIU

M

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TABLE 6.

Determination of Thorium in the presence of Phospha-

Thorium taken Phosphate taken Thorium found Error Percentagemg. mg. mg. mg. error

0.478 2,18 0.471 -0.007 1 .5

0.717 4.90 0,742 +0.025 3 .4

0.239 1.91 0.240 +0.001 0 .0

1.195 10.9 1.135 - 0.060 5 .0

. 0.239 2.5 0.233 - 0.006 2.0

0.717' 5.45 0.755 +0.038 5.2

0.239 1.3 0.238 - 0.001 0.0

C alculation of the above re su lts

mg PO^^ 4 atomic weight PO mg PO x 232,1 mg PO

®-a^ ° Th “ mg Th ” mg Th x 94*98 mg Th X ^ ^atomic ?/eight Th

For the f i r s t re su lt in Table 6 the o p tic a l density reading was 0.365*

From the outermost graphs in F ig . 6 th is reading for o p tica l density g ives

values of 0,430 and 0,525 nig thorium. These figu res g ive s

(a) Ratio = 2.18 x 2.44 = 12 ,4Th 0.430

fb'l Ratio — - 2‘18 * 2- ^ = i n ' ,K ' * Th ~ 0.525 ° The average i s therefore 11 .3 .

Hence 11,3 = ? g ives mS thorium = 0.471*

From the above r e su lts i t would appear that the method i s more accurate in

very d ilu te so lu tio n . ^But even so , the method can hardly be considered r e lia b le .

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-58-

T w o were devised. These are described below s-

( l ) This method makes use of two fa c ts which came to l ig h t during the

course of th is work. These are

( i ) The a b il i ty of thorium to form an anionic complex in n itr ic acid ,

( i i ) The absence of anionic chloride complexes of thorium in hydro­

ch loric acid .

The procedure was as fo llow s - To the so lu tion containing thorium

and phosphate su f f ic ie n t n itr ic acid was added to make the to ta l n itr ic

acid strength of the so lu tion about 8M. N itr ic acid (8M) was then added

u n til the to ta l volume was about 250 ml. This so lu tion was then passed

slow ly down a column of n itra te form DeAcidite FF (water regain = 1 .33)

which had been previously treated with about 200 ml, of 8M n itr ic acid .

The column used was about 10 cm. long and about 2 cm. in diameter. After

passage of the thorium containing so lu tion , the r e s in was washed with 8M

n itr ic acid , u n t il the washings gave no t e s t for phosphate w ith ammonium

molybdate, generally , about 250 ml. o f acid were required. The column

was then e lu ted w ith about 200 ml. of approximately 3M hydrochloric acid .

The elu ate was then evaporated down to about 3“5 m l., d ilu ted with water,

the pH was adjuted to 1 .8 to 2 .0 with ammonia and the thorium t itr a te d

with EoD.ToA. as ind icated above.

The method was checked by taking a known amount of thorium phosphate

so lu tion , the to ta l thorium content of which was known from the weight o f

thorium carbonate taken fo r preparation (See page 36 ) . As can be seen

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-59-

from the r e su lts given in Tables 7 and 8, the method i s very accurate,

and i s sa tis fa c to ry when the PO /Th ra tio i s as high as 1 2 / l .

( l l ) This method i s very sim ilar to that above, but i t has been proved

to be sa tis fa c to ry in a five-hundred fo ld excess of phosphate, To the

so lution containing thorium and phosphate about 350 ml. of a M/2 so lu tion

of disodium hydrogen phosphate was added. The so lution was stirred and

f i l t e r e d immediately. The f i l t r a t io n was carried out at the pump using

a 9 cm.Buchner funnel with a Whatman N o.l f i l t e r paper and very l ig h t

suction . The p rec ip ita te was not washed. The p rec ip ita te and paper were

then transferred to a beaker with 81 n itr ic acid , the funnel was then washed

with 8M n itr ic acid , and the washings added to the beaker.

After standing fo r about h a lf an hour the above so lu tion was f i l t e r e d

through a Whatman No.541 f i l t e r paper. The f i l t r a t e was tran sferred to a

separating funnel and the volume made up to about 250 ml. This so lu tion

was then passed through a column of anion exchange resin (DeAcidite FF,

water regain 1 . 33) in the n itra te form, which had been pretreated with 8M

n itr ic acid . From th is point the method was id e n t if ic a l with that described

above.

The method was checked in the same way as before, i . e . by taking

a so lu tion containing known amounts o f thorium and phosphate. The

resu lts are given in Tables 9 and 10.

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- 60-

TABLE 7.

Determination of Thorium in the presence of Phosphal

R esults fo r a PO /Th ra tio of 3 / l

ate taken Thorium taken ©

Thorium found 6

Error 0.1 mg

0.03 0.0223 0,0223 0

0.03 0.0223 0.0224 +1

0.04 0.0314 0.0314 0

0.04' 0.0314 0.0316 +2

0.05 0.0376 0.0376 Q

0.03 0.0376 0.0373 -3

0.06 0.0436 0.0455 -1

0.06 0.0456 0.0454 -2

0.07 0.0580 0.0580 0

0.07 0.0580 0.0579 -1

— ...................

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ra tio

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- 62-

TABLE 9.

Determination of Thorium in the presence of Phospha-

R esults for a PO /Th ra tio of lOO/l

Phosphate takens .

Thorium taken g- -.

Thorium found g .

E rro rO.lmg.

0.91 0.0223 0.0222 -1

0.91 0.0223 0.0223 0

1.29 0.0314 0.0313 -1

1.29 0.0314 0.0314 0

1 .54 0.0376 0.0376 0

1 .54 0.0376 0.0373 -3

1.87 0.0456 0.0455 -1

1.87 0.0456 0.0455 -1

2.38 0.0580 0.0580 0

2.38 0.0580 0.0579 -1

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-63-

TABLE 10.

Determination o f Thorium in the presence of Phosphate

R esults for a PO /Th ra tio of 500/1

Phosphate taken g •

Thoriuin taken &

Thorium found g. -.

1Error

0 »T m&m

4.57 0.0223 0.0223 0

4.57 0.0223 0.0221 - 2

5.43 . 0.0314 0.0315 + 1

5.43 0.0314 0.0314 0

7.70 0.0376 0.0375 - 1

7.70 0.0376 O.O372 - 4

9 .34 0.0456 0.0456 0

9.34 0.0456 0.0451 - 5

11.88 0.0580 0.0573 - 2

11,88 0.0580 0.0575 - 5

Sim ilar r e su lts were obtained with so lu tion s in which the

P0^/Th ra tio 7/as 250/1 and 400/1.

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~64~

Discussion of Method

The method was found to be su ccessfu l with 10 ml. of a so lu tion

that was M/50 in thorium and 10M in phosphoric acid . The method depends

on the in s o lu b ility in phosphoric acid of the phosphate compound formed

by the addition of the M/2 disodium hydrogen phosphate, and upon the

s o lu b ility of th is compound in 8M n itr ic acid as w ell as the fa c to r s

mentioned previously .

During the course of the work, p rec ip ita tio n of the thorium was

attempted with various concentrations of disodium hydrogen phosphate

ranging from 2M to jj/10. I t Tfas found that Vi/2 gov 3 the nrost

sa tis fa c to ry r e s u lts . Solutions of other concentrations gave somewhat

inaccurate r e su lts , e .g . the resu lts obtained a fter p rec ip ita tio n with 2M

were about 25% low. The resu lts obtained using these various concentra­

tio n s are given in Table 11 and p lo tted in D ig .7.

In addition to the accuracy factor, the p rec ip ita te s obtained with

the higher strength so lu tion s were d if f ic u lt to f i l t e r on account of the

p a rtic le s iz e and those obtained with the le s s concentrated so lu tion s were

completely ge la tin ou s.

I t i s important to f i l t e r the p rec ip ita te e ith er w ithin about h a lf

an hour or a fter fo r ty -e ig h t hours standing. I t was found that in te r ­

mediate times of standing lead to anomalous r e s u lts .

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TABLE 11.

Determination of Thorium in the presence of

% error occurring wi‘ erenof disodium

Strength of disodium hydrogen phosphate

M/10

m/ 4

2M/5

M/2

M

3M/2

2M

fo error

24

14

6

0

6

16

26

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°/o

ERRO

RL .C"Ob**

F IGURE 7

% ERROR AGAINST STRENGTH OF

DISODIUM HYDROGEN PHOSPHATE

FOR SECOND METHOD OF DETERMINING THORIUM IN PRESENCE OF PHOSPHATE

30

EO

OM I-5M EM

MOLARITY OF DISODlUM HYDROGEN PHOSPHATE

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The method has been shown to be sa tis fa c to ry over the range of

thorium concentrations required for th is work.

This method, or one of a sim ilar type, might w ell be applicable to

the determination of thorium in the presence of arsenate.

As can be seen from Table 10 the method i s extremely accurate, the

r e su lts obtained being w ell w ithin the usual lim its required.

Sulphate in the presence of thorium

I t was thought that i t might be necessary to determine sulphate

in so lu tion s containing thorium. The usual method of p rec ip ita tio n with

barium chloride was found to give anomalous r e su lts and la te r th is was

found to be due to the fa c t that thorium i s coprecip itated (81) with the

barium sulphate. Very l i t t l e appears to be known about the process

(82, 83), and i t was thought that i t might prove of some value to in v e s t i­

gate the phenomenon further. This in v estig a tio n forms Part 2 of the

present work.

The determination of sulphate in the presence of thorium was carried

out by taking the so lu tion containing both sp ecies, and ad justin g the pH

to 1 .0 , The pH value of the so lu tion was adjusted with hydrochloric acid

or ammonia. The so lu tion was then passed through a column of ZeoKarb 223

in the hydrogen form. The s iz e of the column was, approximately, 15 cm*

long by 1 cm. in diameter. The thorium was sorbed on to the resin and the

sulphate in the resu ltin g so lu tion was determined in the usual way. The

accuracy of the r e su lts was w ithin the normal lim its required.

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-68-

KESULTS AM) DISCUSSION

G-eneral

Since the cation exchange experiments were concerned with the removal

of thorium ions from the resin phase by an acid , the resu lts have been ex­

pressed as a percentage of the thorium removed from the resin . One advant­

age to be obtained by expressing the resu lts in th is way i s that the resu lts

of d ifferen t se r ie s can be compared without n ecessa rily having the same

quantity of metal on the resin at the beginning. To show that th is was

in fa c t the case, that i s , that d ifferen t degrees of loading were perm issib le,

a se t of experiments were carried out with the thorium form o f ZeoKarb 225*

The resin was loaded to d ifferen t extents with thorium and then id e n t ic a l

ser ie s of equilibrium experiments were carried out in hydrochloric acid

media. The resu lts of these experiments are given in Table 13* These

show that, with down to about 80fo o f the maximum p ossib le loading, the per­

centage of thorium removed under the same conditions was unaltered.

In the case of the anion exchange experiments the resu lts have generally

been expressed as moles per equivalent of re s in . The reason fo r th is i s

th at, when using res in s of d ifferen t water regain , the amount of res in

weighed out i s in fa c t re s in plus water. The resin capacity data take in to

account the water present in the a ir dried resin and the data fo r d ifferen t

ser ie s can then be r e la te d . This fa c t i s c lea r ly il lu s tr a te d by Tables

22 and 24- and F ig s . 13 and 16. Experiments were conducted in order to

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69-

ascertain the amount of water present in a ir dried resin s of d ifferen t

water regains. 1.000 g: . samples of a ir dried DeAcidite FF were taken

and heated to constant w eight in an oven at 110°. I t was found that resin

more water than one of water regain 1.33 dried under sim ilar conditions.

G-raphs; The graphs f a l l in to two groups, those with the cation exchange

work and those connected with the anion exchange experiments, the former

being p lo tted as % thorium removed from the resin against acid pH or molar­

i ty , the la t te r as moles thorium sorbed per equivalent of r e s in against acid

pH or m olarity.

; As a check that the re s in could be f u l ly loaded and that a l l

the metal could be removed on regenerating, some thorium and hydrogen

capacity measurements were made. Starting with the thorium form of the

resin , the metal was q u an tita tive ly removed with 2M n itr ic acid and de­

termined. The resin was then thoroughly v/ashed and the hydrogen capacity

was determined. The r e su lts are given below in Table 12.

of water regain 0 .67 a ir dried at room temperature contained about 10%

TABLE 12.

ZeoKarb 225^

Resin M illi-equivs.T h Mi H i - e qui v s • H

ZeoKarb 225 1.98 1,97

ZeoKarb 225 1.97 1.96

ZeoKarb 225 1.98 1.9^

* Samples weighed as thorium form res in .

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i From previous work carried out in these labora­

to r ie s ( 97) times o f contact of seven days at 20° were f e l t to be adequate

to allow the systems to reach equilibrium, but to be certa in , a ser ies of

experiments were carried out using the thorium form of the resin and

standard acid with times o f contact of seven and fourteen days. I t was

found that equilibrium was in fa c t achieved a fter seven days. The resu lts

are given in Table 14#

( i ) Experiments at various pH’s ; The r e su lts for the equilibrium experiments

performed.with ZeoKarb 225 and hydrochloric, n itr ic , sulphuric and perch­

lo r ic acids at pH values between 0.05 and 1 .5 are given in Table 15 and

p lo tted in F ig .8.

In the case of the experiments with phosphoric and arsenic acids, the

r e su lts , for reasons previously sta ted (see page 3&)> are not equilibrium

values but are the values obtained a fter three or four hours’ shaking.

The r e su lts of these experiments with thorium form resin are to be found

in Tables 16 and 17. The r e su lts are to be found in graphical form in

F ig .9. The data from Tables 16 and 17 being p lo tted as % metal removed

against pH o f so lu tion .

( i i ) Experiments a t various m o la r it ie s : These r e su lts for hydrochloric,

n itr ic , sulphuric, perchloric and phosphoric acids between 1 and 12M are

given in Table 18 and p lo tted in F ig .10. A further se t of re su lts fo r

sulphuric acid a fter four hours shaking are given in Table 19 (for con­

venience side by side with those obtained at equilibrium ) and p lo tted in Fig.

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Generali In general these experiments were-conducted with two resin s ,

DeAcicLite FF of water regain 0,67 and 1.33 f a^d acids of various m olar ities .

Perchloric a c id : The re su lts o f the experiments with perchloric acid are

given in Table 20 and p lo tted in F ig ,12,

N itra te m edia: Experiments were performed w ith bo th n i t r i c a c id and sodium

n i t r a t e so lu tio n , the r e s u l ts being given as m illim oles of thorium sorbed

per gm. of r e s in in Tables 21 and 22, and as moles p er eq u iv a len t in Tables

23 and 24. These re su lts are p lo tted in F igs. 14 and 13.

Chloride media; Experiments were carried out with so lu tions of both hydro­

ch loric acid and sodium ch lorid e. The r e su lts are to be found in Table 23

and they are given in graphical form in .Fig, 13.

Sulphuric a c id : Owing to the fa c t that thorium sulphate was p recip ita ted

in the experiments with 3, 6, 7* 8, 9, 10M sulphuric acid, an incomplete

se t of resu lts only were obtained fo r th is medium,These are given in Table

20 and p lo tted in F ig .11.

Phosphoric a c id : Again p rec ip ita tio n occurred but i t proved p ossib le to

carry out experiments with between 4 and 10M phosphoric acid and these

r e su lts are recorded in Table 26 and p lo tted in F ig ,16,

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Discussion of Results

Cation exchange experiments:

Experiments at various pH values - Reference to F ig ,8 shows that

the amount of thorium removed from the res in i s roughly the same for n it r ic ,

hydrochloric and perchloric acid s. Since perchloric acid i s generally

considered to be the le a s t l ik e ly complex forming agent, then i t i s reason­

able to suppose that the hydrochloric and n itr ic acids do not form complexes

with thorium under these conditions, the removal of thorium probably being

accounted fo r by simple exchange of thorium and hydrogen io n s.

In the case of sulphuric acid , however, the amount of thorium re­

moved i s much greater, being of the order of 91 per cent with sulphuric

acid of 0,03 pH. Since at the concentrations under consideration both

sulphate and bisulphate ions are present, the complex ind icated may be

of the type Th(S0^)f+ or Th(SO^)^ •

As mentioned previously the resu lts fo r phosphoric acid are neither

complete nor do they represent equilibrium values, due to the tendency of

the thorium phosphate to come out of so lu tio n . They do, however, serve as

a guide to the s itu a tio n l ik e ly to p reva il at equilibrium . The data for

th is acid a fter three hours shaking are comparable with those of sulphuric

acid at equilibrium , and a fter four hours the amount of thorium removed

i s even greater. I t i s probable, therefore, that at equilbrium the amount

of complexing would be g rea test with phosphoric acid .

I t i s unfortunate th a t, because of p rec ip ita tio n , re su lts with

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-73 -

arsenic acid were obtainable in the higher pH range only. Even these

r e su lts are not equilibrium values but are values obtained a fter two hours'

shaking. I t i s d i f f ic u l t , therefore, to fo recast what the s itu a tio n would

be at equilibrium . The resu lts are comparable for those obtained with

hydrochloric acid at equilibrium and i t i s reasonable to suppose that i f

arsenic acid experiments could be allowed to reach equilibrium then the

amount of thorium.removed would be greater with arsenic acid than with

hydrochloric acid .

formation, under the conditions of the above experiments, may be deduced :

In F igs. 10 and 11 the r e su lts at various acid m olarities are

recorded. For both n itr ic and hydrochloric acid r e su lts a peak in thor­

ium removal i s observed at about 6M which in d icates that complex formation

i s probably greatest at that region. The peak in thorium removal at

about 2M acid concentration recorded for perchloric acid i s rather lower,

and in view of the acid concentration at which i t occurs i s l ik e ly to be

associated with changes in the hydrogen ion a c t iv ity .

The re su lts fo r sulphuric acid are incom plete. I t can be assumed,

however, on the b asis of the r esu lts shown on the graph in F ig .11, that

the general shape of the curve at equilibrium would be that indicated by

From these considerations the follow ing general order of complex

or

H9S°, \ H AsO, HC10

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-7 4 -

the broken l in e . Evidence in support of th is view i s provided by data

obtained fo r four hours shaking which has the same general shape.

Returning to F ig .10 and the phosphate r e su lts , i t can be seen that

there are only three points on the curve. Taking into consideration the

r e su lts shown in F ig .8, i t can be assumed that the curve would have the

shape shown in F ig ,10, that i s , a stra igh t l in e at about 38%> thorium removed.

This i s in d ica tiv e of strong complex formation throughout the range of con­

centration studied.

These graphs would suggest that in strongly acid so lu tion , the order

of complex formation i s , very generally :

H,P0, HC1 HNO, HoS0, HC10.3 4 3 2 4 4

Anion exchange experiments

F ig .12 shows the uptake of thorium from perchloric acid . As can

be seen the uptake i s very small and i s constant throughout the range of

concentration studied.

The resu lts obtained with sulphuric acid are also shown on th is

fig u re . As previously mentioned, the resu lts are incomplete owing to the

p rec ip ita tio n of thorium sulphate. In order to try and obtain additional

r e s u lts , the volume of sulphuric acid used was doubled and the amount of

thorium added was halved, but p rec ip ita tio n again occurred. However, the

points shown on the graph in d icate that as the sulphuric acid concentration

increases the tendency of thorium to form anionic complexes in creases.

These experiments were conducted with resin s of water regain 0.67

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-7 5 -

and 1 .33 , the r e su lts showed that there was no appreciable d ifference in

the amount of thorium taken up per equivalent of resin .

On the b a sis of these re su lts i t i s probable that a b isulphate

complex o f thorium i s being formed since the ra tio of bisulphate increases:

with increasing acid concentration.

F ig s . lif and 15 show the resu lts with n itra te so lu tions p lo tted

both as m illi-m oles of thorium sorbed per g • dry resin against m olarity

of so lu tio n , and as moles of thorium sorbed per .equivalent of resin

against m olarity of so lu tio n . These graphs i l lu s t r a te the point already

made e a r lie r that the amount of a ir dried resin obtained when resin s of

d ifferen t water regain are weighed out i s not exactly the same. The.

difference i s due to the amount of water held by the re s in , With the

resin s used in these experiments, th is d ifferen ce was of the order of

8 - 9^. G-raphs 2 and 3 in F ig . 1^ show that the d ifference in the r e su lts

i s of that order, and F ig .15 shows that these graphs in fa c t coincide i f

allowance i s made fo r th is d ifferen ce in weight of actual resin by con­

sidering moles o f thorium sorbed per equivalent of resin .

Considering the re su lts shown graphically in F ig .15, several impor­

tant points emerge

Graph 2 i s the r e su lt of experiments w ith n itra te form res in ,

n itr ic acid and thorium n itra te so lu tion . Here the amount o f thorium

taken up in creases s tea d ily w ith r is in g acid concentration u n t i l a maximum

i s reached at about 8M n itr ic acid . The amount sorbed then tends to

f a l l slow ly. These r e su lts are in good agreement with the work of

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Da non ( 65), who suggested maximum complex formation at strengths of

n itr ic acid greater than 7M, but are in opposition to statements by Hyde

( 6 l ) , and a lso of Katz and Seaborg (62)• They are also in c lo se agreement

with a very recent paper on the a n a ly tica l aspects of anion exchange by

Binney e t a l (85)* These authors ind icated that maximum complex formation

occurs at about 8M n itr ic acid . This i s in d ica tiv e of anionic complex

formation, the tendency being strongest at about 8M. ALtJiough i t i s

possib le th at the s lig h t fa l l in g o ff in uptake at concentrations greater

than 8M i s due, in part at le a s t , to s lig h t degradation of the resin at

high acid concentrations, i t i s possib le th at the complexes formed may

be Th(N0^)5“and ThtNO.^*.

Two re s in s were used w ith the id ea th a t i f the complex anion formed

was la rg e the more t ig h t ly c ro ss - lin k e d re s in would a c t as a s ieve and th e

amount o f thorium sorbed would be le s s . A lte rn a tiv e ly , i f two o r more

complexes were formed and th ese d if f e re d considerab ly in s iz e , then again

the sieve e f f e c t of the r e s in may have produced d if f e re n t r e s u l t s . In

f a c t , th e r e s u l t s ob tained were the same in both cases, and so i t can be

assumed th a t th e complex o r complexes formed are no t la rg e . This would

in d ic a te Th(NO^)^ o r Th(NO^)^5*.

Graph. 1 in F ig .15, shows the r e su lts of sim ilar experiments con­

ducted with chloride form DeAcidite FF and n itr ic acid . This i l lu s t r a te s

c lea r ly the e f fe c t of a ’foreign ' ion in the system. The graph fo llow s

the same trend as that of Graph 2, reaching a peak at about 8M n itr ic acid ,

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the amount of thorium sorbed, however, i s c o n s is te n tly h ig h er throughout

the range* This may be due to a combination of two th ings I

( i ) When weighing the r e s in the a c tu a l amount of r e s in ob tained j

(as opposed to w ater and gegen io n ) in the ch lo rid e form i s probably s lig h tly ,

g re a te r than the amount ob ta ined in the n i t r a t e form, due to the d i f f e r e n t !

w eights of these io n s .

( i i ) The a f f in i t y of th e n i t r a t e io n f o r the re s in i s g re a te r than

th a t of the ch lo rid e ion and i t may be th a t the complex formed has a r e la t iv e ”

ly h igher a f f i n i t y than the ch lo rid e io n .

The resu lts of the experiments in sodium n itra te media are shown in

Graph 3 in F ig .15. I t was not p ossib le to use concentrations of sodium

n itra te greater than 6M because saturation point i s reached soon afterwards. j

Once again the r e su lts fo llow the trend of the other graphs in that the

amount of thorium sorbed r is e s with increasing n itra te concentration. This

shows that the complex formation i s not dependent on large hydrogen ion

concentrations.

F ig .13 shows the r e su lts fo r chloride media. As can be seen the

amount o f anionic complex formation in th is medium i s n e g lig ib le . These

re su lts are in agreement with the work of Kraus, Mo'are and Nelson ( 60) ,

although these authors made use of hydrochloric acid and lithium ch lorid e.

Here again experiments with resin s of d ifferen t water regain were performed

for the same reason as before.

Graph 1 in th is figu re i s the r e su lt of using thorium n itra te so lu tion

in place of thorium so lu tio n . The graph shows the considerable e f fe c t that

the presence of a ’fo re ig n ’ anion can have on the complex formation.

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The thorium that was taken up was probably sorbed in the form of a n itra te

complex, th is being the only p ossib le e f fe c t of the addition of a small

amount of n itra te ion . There i s no reason to suppose that the presence of

a f o r e ig n 1 ion in an in v estig a tio n in to the ca tion ic complexes of a metal

would not have a sim ilar profound e f fe c t on the system, and i t i s fo r th is

reason that some of the r esu lts o f Schulz and Herak ( l 3) are open to doubt.

These authors in v estig a ted by means of the cation exchange resin Anberlite

IR-120 the ca tio n ic complexes formed in various acid media, e .g . H^SO and

HC1. The thorium was present in the so lu tion s used, as thorium n itra te

(see page 29)*

The. r e su lts shown in F ig .l6 are those obtained in phosphoric acid

so lu tio n . The maximum amount of thorium sorbed was at about 5M phosphoric

acid . The graph i s again the r e su lt of two ser ies of experiments with

resin s of d ifferen t water regain, the r e su lts again being the same,

A consideration of the cation exchange re su lts would ind icate that

there i s a large degree of complex formation. The anion exchange r e su lts

would lead to the conclusion that anionic complex formation i s small and

that i t i s maximum at about 5M. To cover both of these s e ts of r e su lts i t

i s necessary to postu late an uncharged ion*

I t has been suggested by Schwarzenbach (96) that thorium phosphate

e x is ts as a three-dim ensional cross-lin k ed structure. In phosphoric acid

so lu tion of increasing strength i t i s p ossib le that such a structure may break

^ 5 -down to give complex anions of the type |jTli(PO ) an<

Complex anions of th is type may be sorbed by the r e s in . At concentrations

greater than 5M phosphoric acid these complex anions might be converted to un­

charged or low charged complexes of the type ^ (H P O ^g or ^Th(HP0^)^| •

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T A B U L A R R E S U L T S f or P A R T I

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TABLE 13.

The removal of thorium with hydrochloric acid from

ZeoKarb 225 with d ifferen t degrees of loading a fter seven

days contact.

Temperature.. . . . . . . . . . 20°C (-3 )

Resin . . . . . . . . . . . . . . . .approximately 10% D.V,B„, W.R, about 0 .7 .

Capacity of resin . . . . 3 . 9 6 m illi-e q u iv s . T h /g .d r y re s in .

Volume of so lu tion . . . 5 0 ml.

Weight of res in . . . . . . 0 . 5 0 0 g. (weighed as thorium form).

Loading in m .eq./0.500 g . of r e s in (Thorium form) 1.93 1.80 1.69

Loading as % of max. 100 93.3 87.6

PH tho]?ium removed %

0.05 46 46 45

0.25 37 36 37

0.50 30 31 29

0.75 26 26 26

1.00 24 23 24

1.25 17 18 18

1.50 16 15 17

1.54

79.8

47

35

30

25

23

17

16

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81-

TABLE 14.

The removal of thorium from ZeoKarb 225 with hydrochloric

acid fo r times of contact of seven and fourteen days*

Temperature............. » . . « .............20°C ( - 3 )

R e s in .................... ...........................About 10% D.V.B., WeR* about 0.7*

Weight of res in ............. 0.500 g.

Total Thorium ...................... 1.59 m illi-e q u iv s ./0 .5 0 0 g .. r es in .

Volume of so lu tion ................. 50 ml.

pH Thorium removed from res inA fter 7 days A fter 14 days

0.05 46 45

0.25 37 37

0.75 31 31

1.00 2.6 25

1.25 25 24

1.50 17 17

1.75 16 16

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TABLE 15.

The removal of thorium from ZeoKarb 225 with various

acids at several pH values a fte r seven days contact.

Temperature ......... .. 20°C (-3 )•

Resin . , ............. . ...................10$ D0V0B., W»Ro 0,7 about.

Weight of resin ...................... 0,500 g.

Total Thorium 1,59 m illi-e q u iv s ./0 ,5 0 0 g . resin .

Volume of so lu tion .........50 ml.

Thorium removed $

pH HC1 HN0,j

*

H2S04 HC10,k-

0.05 46 48 91 36

0.25 37 39 83 33

0.50 31 31 67 29

0.75 26 26 49 25

1.00 25 23 39 24

1.15 - - 39 -

1.25 17 21 38 22

1.40 - - 34 -

1.50 16 17 31 18

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-83 -

TABLE 16.

Removal of metal from thorium form ZeoKarb 225 with phosphoric

acid at various pH values a fter 3 and 4 hours shaking.

Temperature ............... 20°C (~3).

Resin .................. . . . . . . W a t e r regain 2.04-.

Weight of res in .......... .0 .500 g.

Capacity of resin 1 .810/0 .500 g.

Volume of so lu tion . . . . . . . 5 0 ml.

pH Thorium removed fo

a fter 3 hours shaking a fte r 4 hours shaking

0 .6 80 98

0.25 77 95

0.37 75 ❖

0.50 *

0.72 * *

0.96 *

1.23 * ❖

1.48 13

*Denotes th at p rec ip ita tio n was observed.

Sim ilar experiments were conducted with r e s in of water regain 0 .67 .

The r e su lts were s l ig h t ly lower than those given above.

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-84 -

TABLE 17.

Removal of metal from thorium form ZeoKarb 225 with arsenic

acid at various pH values a fter 3 and 4 hours shaking ,

Temperature . . • • • • . . . . •. • • 20°C (-3 ) •

Resin ......... . . Water regain 2.04*

Weight of res in ............. 0.500 g.

Capacity o f resin . . • • • • • , 1 .810/0 .500 g.

Volume of so lu tion • • • • . • • 50 ml.

PH Thorium removed % j

a fter 3 hours shaking a fter 4 hours shaking,

0.05 *

0.32 * *

0.55 * *

0.99 * *

1.30 16 23

1.50 12 16

1.72 5 8

^Denotes that p rec ip ita tio n was observed.

Sim ilar experiments were performed with resin of w ater regain 0 .67 .

The re su lts obtained were s lig h t ly lower than those given above.

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-85-

TABLE 18.

The removal of thorium from ZeoKarb 225 with various

acids at several m olarities a fter seven days con tact.

Temperature 20°C(-3)«

R e s in ........................ ..... 10$ DoV.B., ¥ 0R. about 0 .67.

Weight of resin ............. 0.500 g.

Capacity o f r e s in . . . . . . . . 1.73 m illi-eq u iv s ./0 ,5 0 0 g: • res in .

Volume of so lu tion . . . . . . . 50 ml.

Molarity Thorium removed $

HC1 HNQ,j H2S04 HC10,4 H,P0, 3 4

1 71 46 95 47 *

2 82 63 90 57 *

3 92 84 80 56 *

6 96 99 * 21 98

9 93 94 * 5 97

12 - 81 0 0 98

# Denotes that p rec ip ita tio n occurred before equilibrium had been attained.

Additional experiments were performed with 5M and 7M hydrochloric acid ,

these removed 96 and. 97 per cent thorium resp ectiv e ly .

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-86

Table 19.

The removal of thorium from ZeoKarb 225 with sulphuric acid at

several m olarities a fte r seven days standing and a fter 4 hours shaking,

Temperature • • ........................ 20°C (-3 ) *

R e s in ......................................... 10% D.V0B., W0R. about 0 .67 .

Weight of resin ............. 0.500 g.

Total th oriu m ...................... 1.73 m illi-e q u iv s ./0 .5 0 0 g . res in .

Volume of s o lu t io n ............. 50 ml.

Molarity Thorium removed %

i 7 days standing

1 I 93 93

2ij 90 86

3 1 80!

78

6i1 * 46

9 1 * 9

12 0 0

4 hours shaking

* Denotes that p rec ip ita tio n occurred before equilibrium had been atta ined .

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-87-

TABLE 20.

The sorption of thorium from sulphuric and perchloric acid so lu tion s

by means of the anion exchanger DeAcidite FF a fte r seven days standing.

Temperature................... 20°C (-3).

Resin Capacity ............. Yfater regain 0 ,67 , 3*26l m illi-e q u iv s ./g •

Water regain 1.33> 3*926 m illi-e q u iv s ./g *

Weight of res in taken,, l.OOOg,

Volume of so lu tion . . . . 50 ml.

Moles of thorium sorbed per equivalent of res in

Acid Sulphuric Perchloric

Resin DeAcidite FF sulphate form

DeAcidite I fo?

T perchlorate rm

Molarity of acid

W.R. 0.67 W.R. 1.33 W.R. 0.67 W.R. 1.33

1 0.003 O.OOlf 0.003 0.002

2 0.006 0.007 0.003 0.002

3 ,0.017 0.017 0.002* 0.001

k * * 0.002 0.002

5 * * 0.002 0.002

6 0.002 0.002

7 * * 0.003 0.003

* Denotes p rec ip ita tio n occurred before equilibrium had been atta ined .

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-8 8 -

TABLE 21.

The sorption of thorium from n itr ic acid so lu tion by means of the

anion exchanger DeAcidite EE a fter seven days- standing.

Temperature .................... 20

Resin Capacity Water regain 0.67, 3.261 m illi-e q u iv s ./g •

Yfeter regain 1 . 33, 3*926 m illi-e q u iv s ./g •

Weight of res in . . . . . . . 1.000 g.

Volume of s o l u t i o n . . . . . 30 ml.

Resin DeAcidite FF n itra te form DeAcidite FF chloride form

W.R.0.67 W.R. 1.33 W.R. 0.

Acidm olarity

m illi-m oles thorium sorbed per g •. dry resin

1 0.009-

0.019 0.139

2 0.016 0.019 0.189

3 0.039 0.074 0.241

4 0.209 0.251 0.362

5 0.346 0.404 0.520

6 0.489 0.600 0.649

7 0.616 0.742 0.763

8 0.652 0.781 0.767

9 0.639 0.7^9 0.750

10 0.603 0.722 0.711

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-8 9 -

TABLE 22.

The sorption of thorium from sodium n itra te so lu tion .b y means

of the anion exchanger DeAcidite FF a fter seven days standing.

Temperature ........................ 20°C(-3).

Resin c a p a c ity 3*261 m illi-e q u iv s ./g ..

Resin water regain . . . . . 0.67

Weight of res in ........... .. 1.000 g.

Volume of s o lu t io n 50 nil.

Molarity of sodium n itra te

1

2

3

4

5

6

M illi-m oles thorium sorbed per g , dry resin

0.000

0.016

0.062

0.267

0.316

0.453

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TABLE 23.

The sorption of thorium from n itr ic acid so lu tion by means of the

anion exchanger DeAcidite FF a fter seven days standing*

Temperature ....................... 20°C(-3).

Besin c a p a c ity .................. Water regain O.67, 3*26l m ill i- e q u iv s ./g •

Water regain 1 .3 3 9 3*926 m illi-e q u iv s ./g .

Weight of r e s i n 1,000 g.

Volume of s o lu t io n 50 ml.

Acidmolarity

1

2

3

4

5

6

7

8

9

10

Moles thorium sorbed per equivalent of res in

B esin; DeAcidite FF n i t r a t e form

Besin: DeAcidite FF ch lo rid e formW.B. 0.67i/?.B. 0.67 W.B. 1.33

0.005 0.0430.003

0.0580.005 0.005

0.018 0.0740.019

0.111

0.103

0.153 0.1990.150

0.224

0.2330.1990 .200

0.230

0.2180.184

i

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-91-

TABLE 24.

The sorption of thorium from sodium n itra te so lu tion by means

of the anion exchanger DeAcidite FF a fter seven days standing.

Temperature ............. .. 20°C (-3).

Resin capacity ............. .. 3.261 m illi-e q u iv s ./g •

Resin water regain . . . . . 0,67.

Weight of res in ............... 1,000 g.

Volume of so lu tion ......... 50 ml.

Molarity of sodium n itra te

Moles of thorium sorbed per equivalent of r e s in .

1 0.000

2 0.005

3 0.019

4 0.063

3 0.097

6 0.139

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-92 -

TABLE 25.

The sorption of thorium from hydrochloric acid so lution by means

of the anion exchanger DeAcidite FF a fter seven days standing.

Temperature ....................... . 20°C(~3)*

Resin capacity . . . . . . . . . . Y/ater regain 0.67, 3*261 m illi-e q u iv s ./g .

Water regain 1,33> 3*926 m illi-e q u iv s ./g •

Weight of res in ............... 1.000 g.

Volume'of so lu tion ........... 50 ml.

Acidm o larity

Moles thorium sorbed per eq u iv a len t of r e s in

Thorium n i t r a t eThorium so lu tio n ?

Thorium ch lo rid e Thorium ch lo rid e

Resin DeAcidite FF ch lo rid e form

Yv.R. 0b7 " "” ~ 1 0 7 T 3 S

1 0.000 0.000

2 0.001 0.000

3 0.000 0.000

4 0,000 0.001

5 0.000 0.000

6 0.000 0.000

7 0.000 0.000

8 0,001 0.001

9 0.002 0,003

Yv.R.0.£>7.

0.044

0.004

0.044

0.038

0.037

0.037

0.040

0.039

0.038

S im ila r experim ents performed bu t w ith sodium ch lo rid e so lu tio n s gave

id e n t ic a l r e s u l t s .

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-93-

TABLE 26.

The sorption of thorium from phosphoric acid so lu tion by

means of the anion exchanger DeAcidite FF a fter seven days standing*

Temperature *.......... . . . . . . . 20°C(-3)»

Resin Capacity ........... .. Water regain 0*67, 3*26l m illi-e q u iv s ./g •

Water regain 1*33, 3*926 m illi-e q u iv s ./g .*

Weight o f r e s i n ............ .. 1,000 g.

Volume of so lu tion . . . . . . 30 ml.

Resin DeAcidite FF phosphate form

M olarity of Phosphoric

a c id

4

5

6

7

8

9

10

W.R. 0.67 W.R. 1.33

m-moles thorium sorbed per equivalent of resin

0.034

0.080

0.038

.0.023

0.002

0.001

0.000

0.035

0.080

0.040

0.025

0.002

0.001

0.000

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5/0 OF

TH

ORI

UM

RE

MO

VE

D

F I G U R E 8REMOVAL OF THORIUM FROM Z E O K A R B 2 2 5

BY, ACIDS AT VARIOUS pH VALUES

SULPHURIC ACID O NITRIC ACID♦ PERCHLORIC ACID

▲ HYDROCHLORIC ACID• PHOSPHORIC ACID. 3 HOURS

a ARSENIC ACID. 3 HOURSS PHOSPHORIC ACID, 4 HOURS

Q’25 0'S 0-75 1-00

f>H OF SOLUTION

■25 1-5

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°/0

THO

RIU

M

RE

MO

VE

DFIGURE 9

REMOVAL OF METAL FROM THORIUM FROM ZEOKARB 8S5 W ITH PHOSPHORIC

& ARSENIC ACID % R E M O V E D A G A I N S T p H V A L U E

^ O P H O S P H O R I C A C I D 4 H O U R S S H A K I N G® P H O S P H O R I C A C I D 3 H O U R S S H A K I N G

\ A A R S E N I C A C I D \ .▲ A RSEN IC ACID

3 H O U R S S H A K I N G4 H O U R S S H A K I N G

0 ' 2 5 0 -5 0 7 5 10jbW VALUES

l'2 5

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THO

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RE

MOV

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PER

CE

NT

AG

E

F I G U R E 10REMOVAL OF THORIUM FROM ZEOKARB 2 2 5 BY MEANS OF ACIDS AT VARIOUS M O LA R IT IE S 7 DAYS S T A N D IN G

100

90

O HYDROCHLORIC ACID • PERCHLORIC ACID □ NITRIC ACID B PHOSPHORIC ACID A SULPHURIC ACID A SULPHURIC ACID. WITH

3 HOURS SHAKING60

A C ID M OLARITY

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F I G U R E 11REMOVAL OF THO RIUM FROM ZEOKARB 2 2 5 BY MEANS OF SULPHURIC ACID AT VARIOUS MOLARITIESSEVEN DAYS S TA N D IN G A ND TH R EE HOURS SHAKING

▲ 7 DAYS STA N DING

• 3 HOURS SH A K IN G0'9

0'8

P 0 7

0'4

ACID MOLARITY

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-99 -

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MIL

LI-M

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S

OF

THO

RIUM

S

OR

BE

D/G

. DR

Y R

ES

/N

— - —

F I G U R E 14GRAPHS OF MILLIMOLES OF THORIUM SORBEDfBY DEACIDITE FF)

AGAINST NITRATE CONCENTRATION

0 DEACIDITE FF NITRATE FORM W.R. 1-033 N ltR lC ACID SOLUTION

© D E A C ID ITE FF CHLORIDE FORM W .R O ‘67 NITRIC ACID SOLUTION

© DEACIDITE FF NITRATE FORM W,R 0-67 NITRIC ACID SOLUTION

@ DEACIDITE FF NITRATE FORM W.R. 0*67 SODIUM NITRATE SOLUTION

0-8

0-7

0*5

0-4

0-3

o-a

MOLARITY OF N ITR IC ACID OR SO DIUM NITRATE

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MO

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tho

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so

rbe

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of

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in

FIGU RE 15GRAPHS OF M OLES SORBED PER EQUIVALENT OFRESIN A G A IN S T M O L A R IT Y OF N ITR IC ACID OR

SODIUM N ITR A TEGRAPH I - CHLORIDE FORM RESIN WR. O S7 NITRIC ACID SOLN. GRAPH 2 - NITRATE FORM RESIN W.R. 0-678,1-33NITRIC ACIOSOLN. ! GRAPH 3 - NITRATE FORM RESIN W.R 1-33 SODIUM NITRATE SOlN. !•25

•10

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MOLARITY OF NITRIC ACID OR SODIUM NITRATE

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MO

LES

OF

THO

RIUM

SO

RPED

PE

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EQU

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LEN

T OF

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IN

FIGURE 16

GRAPH OF MOLES THORIUM SORBED PER EQUIVALENT OF RESIN AGAINST MOLARITY

OF PHOSPHORIC ACID

THE GRAPH REPRESENTS THE RESULTS OBTAINED W ITH RESINS OF W ATER R EG A IN 1-33 S, 0 - 6 7

1-0

05

00 92 3 4 5 6 7 6 10

MOLARITY OF PHOSPHORIC ACID

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-103-

P A R T II

COPRECIPITATION STUDIES OF THORIUM AND

BiiRIUM SULPHATES

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-104-

HISTORICAL

The phenomenon of co -p recip ita tion has been the subject o f consider­

able d iscussion in the lite r a tu r e , K olthoff having published one se r ie s

of about 50 papers on the top ic between 1930 and 1948* Several papers

(81) - (87) re la te to the co-p recip itation of various ions with barium

sulphate but there are few d ir e c t ly connected with the present work. The

most important of these are three early papers Yfhich are the resu lts of work

by Kammer and Silverman ( 8 l ) , Balcar and Stegeman (82), and of Vasil*eva

(83)* No further work appears to have been carried out on the problem but

the phenomenum.ns mentioned again in papers by Yamamoto (86) and Tezak (87).

The papers of major in te r e s t are those by Kammer and Silverman, and

by Balcar and Stegeman, the former i s e n t it le d ’Adsorption and Ionium-Thorium

by barium sulphate* and the la t te r ’Adsorption and so lu tion phenomena en­

countered in p r e c ip ita tio n s ’ .

The work of Kammer and Silverman (81) may be summarised as follow s

Pure so lu tion s of thorium chloride and barium chloride were prepared, known

portions mixed and the barium p recip ita ted as sulphate by the addition of

sulphuric acid . The thorium remaining in so lu tion was determined (method

not stated ) and the amount adsorbed was found by d ifferen ce. For a constant

amount of thorium and varying amounts of barium ch loride, the re su lts show a

rapid absorption at f i r s t with a tendency to le v e l o ff at higher concentra­

tion s of barium.

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-105-

A sim ilar so lu tion was taken with the barium concentration constant

and the amount of thorium as the variab le . I t was found that the adsorption

was almost independent of d ilu tion and i f anything decreased on d ilu tio n ;

th is i s in contradiction to predictions made on the basis of the Freundlich

isotherm. The conclusion reached was that when barium sulphate i s pre­

c ip ita ted in so lu tions containing thorium, the thorium i s adsorbed to a

remarkable degree. I t was suggested that when the ratio of thorium oxide

to barium sulphate was 1:28, approximately 80$ of the thorium was ”adsorbed”.

The paper by Balcar and Stegeman (82) i s a more d eta iled and extended

study of the work commenced by Kammer and Silverman. The follow ing i s

a b r ie f abstract.

( i ) R e-solution o f thorium adsorbed by barium sulphate. The time,

to reach equilibrium was determined by taking so lu tions having the.same-'

thorium concentration, adding equal amounts of barium chloride and s u ff ic ie n t

sulphuric acid to precipitate- the barium as sulphate. The mixtures were

agitated fo r varying periods o f tim e. I t was found that the amount ad­

sorbed increased with tim e.

( i i ) E ffect of thorium concentration on p a r tic le s ize of barium sulphate<

Solutions containing varying amounts o f thorium and the same amount of barium

chloride were taken. The barium was p recip ita ted by an equivalent amount

of sulphuric acid and allowed to s e t t le in N essler tubes. The re su lts

showed that the rate of s e t t l in g reached a minimum when the thorium concen­

tration was 0.002N, slowly rose to a maximum and then f e l l gradually. At

high concentrations the p rec ip ita te did not s e t t l e appreciably over a number

of days.

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- 106-

( i i i ) The so lu tio n of barium su lphate and lead su lphate in thorium

ch lo rid e s o lu tio n . In the f i r s t s e r ie s of experim ents ( i ) above, i t was

found th a t p r e c ip i ta t io n was incom plete, th e re being only a s l ig h t c loud iness

which d isappeared on warming. Experiments were th e re fo re conducted in

which so lu tio n s o f thorium were prepared and to th ese were added eq u iv a len t

so lu tio n s of barium c h lo rid e and su lp h u ric ac id , a l te r n a te ly drop by drop

from b u re t te s . The so lu tio n was illu m in a te d by a converging beam of l ig h t ,

the end p o in t being taken as the f i r s t appearance of a Tyndall e f f e c t . A

graph of log ( s o lu b i l i ty of barium su lphate )(= log S) a g a in s t log (concen­

t r a t io n of thorium ch lo rid e )(= log c) was p lo t te d and found to be a s tr a ig h t

l in e w ith equation lo g S = n log C + K where n and K are co n s ta n ts . The

s o lu b i l i ty of barium su lphate in thorium ch lo rid e could th e re fo re be expressed

in the form S = KCn (c f F reundlich Iso therm ). S im ila r experim ents were

conducted w ith thorium and lead su lp h a te . The au tho rs reached the con­

c lu s io n th a t complexes were formed bu t th a t they were no t c le a r ly defined .

( iv ) E quilibrium co n d itio n s in a so lu tio n of barium sulphate in

thorium c h lo r id e . These were s tu d ied by tak in g so lu tio n s con ta in ing equal■mnniriM! ■ n m i i ■ nn ■ m i M i i w i a i ..... w w

amounts of thorium and varying co n cen tra tio n s o f barium ch lo rid e and p re ­

c ip i ta t in g Yfith su lp h u ric a c id . The conclusion was reached th a t a simple

equ ilib rium between a complex and i t s ions d id no t e x is t .

(v) A dsorption of thorium by barium su lp h a te . The procedure used

was to take so lu tio n s con ta in ing varying amounts of thorium ch lo rid e and

barium c h lo r id e , and to add to these s u f f ic ie n t su lp h u ric ac id (w ith

s t i r r in g ) to p r e c ip i ta te a l l th e barium. The p re c ip i ta te was removed by

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c en tr ifu g in g and the c le a r supernatan t l iq u id analysed f o r thorium hy

p re c ip i ta t io n as oxala te and ig n it io n to the oxide. The conclusion

was reached th a t w ith p r e c ip i ta t io n of d if f e r e n t amounts of barium su lp h a te ,

the adsorp tion of thorium ch lo rid e v a r ie s somewhat in the same manner as

the s o lu b i l i ty of barium su lphate v a r ie s w ith co n cen tra tio n o f thorium

c h lo r id e .

A paper by K olthoff (88) d ea lin g w ith the theory of c o -p re c ip ita t io n

suggests th a t the amount of c o -p re c ip ita te d ions decreases w ith the tim e of

stand ing before f i l t r a t i o n . This appears to be in c o n tra d ic tio n to B alcar

and Stegeman,(i) above.

V asil'eva (83) noted that when barium sulphate was p recip itated by

adding barium ions to an acid so lu tion containing sulphate, the p rec ip ita te

contained thorium and uranium ( i f Th and UO were present in t h e . o r ig in a l

so lu tio n ). I t was suggested that complex sulphates of barium and thorium

were formed.

Yamamoto (86) conducted an in v e s tig a tio n in to the e f f e c t of the con­

c e n tra tio n of s o lu tio n s , the o rder of mixing and the presence of fo re ig n

ca tio n s (in c lu d in g thorium ) on the p r e c ip i ta t io n of barium su lp h a te . I t

4+was found th a t Th h inders the growth of c r y s ta l s .

Tezalc (87) in a paper dealing with the p rec ip ita tio n of barium su l­

phate p rec ip ita te s , in d ica tes that th oriu ^ i f present in s u ff ic ie n t

q u a n tities, p ep tizes the methoric layer.

Imre and Nagy (89) used thorium B as an in d ic a to r in th e study of

barium su lphate r e c ry s ta l l i z a t io n due to i t s p roperty of ad so rp tio n by the

p re c ip i ta te d barium su lp h a te .

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SCOPE OF THE WORK

Very l i t t l e appeared to be known of the co -p recip ita tion of

barium and thorium sulphates and the object of th is work was to try

and elucidate under 7/hat conditions th is was favoured and, i f p o ssib le ,

fin d out whether, as had been suggested e a r lie r , there were any complex

compounds formed.

S o lu tions of thorium and barium were taken and su lphuric ac id was

added to p r e c ip i ta te the barium as su lp h a te . The amount o f thorium

in the p r e c ip i ta te was determ ined and various graphs were p lo tte d .

As a r e s u l t of these experim ents c e r ta in conclusions were reached, and

i t was f e l t th a t the p o s it io n might be fu r th e r e lu c id a te d by means of

X-ray C rysta llog raphy . Accordingly, powder p ic tu re s were taken by .

the Debye-Scherrer method.

I t proved im possible to e lu c id a te the p o s itio n f u l ly b u t con­

c lu sio n s have been drawn and some suggestions made f o r fu tu re work.

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X-RAY CRY ST ALLQG-RAPHY

AN INTRODUCTION

T h eo re tica l C onsidera tions: Atoms, ions and m olecules in so lid s u su a lly

pack re g u la r ly w ith long range o rd er. Such atomic assem blies are knoY/n

as c ry s ta ls . These have the power to ac t towards X-rays in a manner

s im ila r to a d i f f r a c t io n g ra tin g in o p tic s . Thus, i f a c ry s ta l i s p laced

in the pa th of a beam of X -rays, i t i s p o ssib le to o b ta in a d if f r a c t io n

p a t te rn .

Substances w ith d i f f e r e n t c r y s ta l l in e s tru c tu re w i l l produce d if f e r e n t

X-ray p a tte rn s . Thus, i f a c ry s ta l l in e sample i s i r ra d ia te d by monochromatic

X -rays, the r e s u l t in g d if f r a c t io n p a t te rn w i l l c o n s is t o f an ensemble of

r e f le c t io n s whose angular p o s itio n s are defined by th e wavelength of the

rays and th e spacings of the l a t t i c e p lan es . I t w i l l th e re fo re be unique

in much th e same way as th e ensemble o f ang les bet?/een the faces i s unique.

In ad d itio n to th i s , the in te n s i t i e s of the in d iv id u a l r e f le c t io n s w i l l be

governed by the c h a r a c te r is t ic atomic groupings w ith in the c r y s ta l . Thus,

w ith very few exceptions i t may be in fe r re d th a t no two X-ray d i f f r a c t io n

p a tte rn s w il l be the same in a l l d e ta i l s .

Hull in 1919 (90) stated , ’’every c r y s ta llin e substance g ives a pattern

the same substance always gives the same pattern; in a mixture of substances,

each produces i t s pattern independently of the others; so that the photo­

graph obtained with a mixture i s the superimposed sum of the photographs

that would be obtained by exposing each of the components separately fo r

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the same length of time. This law applies q u an tita tively to the in te n s i­

t ie s of the l in e s as w ell as th e ir p o s it io n s .”

There are three main ways of obtaining and recording X-ray d iffra c tio n

patterns. These are :-

( i ) Laue Method (91): th is method involves a beam of X-rays

containing a range o f wavelengths, impinging on a s in g le stationary c r y s ta l,

the pattern u sually being received on a f la t film .

( i i ) Debye-Scherrer Method (92): th is involves the use of a

powdered specimen and monochromatic rad iation , the pattern being obtained

on a cy lin d r ic a l film .

( i i i ) Rotation or O sc illa tio n Method (93): th is method makes use of

a s in g le cry sta l which i s o s c il la te d or rotated in a beam of monochromatic

X-rays.

The method used for the id e n tif ic a t io n of m aterials i s that of Debye

and Scherrer and was the method adopted for the present work. The method

i s considered in more d e ta il below.

recorded as l in e s , th is being the most convenient type of X-ray d iffra c tio n

pattern fo r id e n tif ic a t io n purposes. The lin e s appear in ascending order

of Bragg angle, & or since X a2dsin(^ in order of descending interplanar

spacings, d. F ig . 17 shows the way in which the Debye-Scherrer pattern i s

produced.

Method.: In a powder diagram the d iffra ctio n e f fe c t s are

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P ra o tic a l Aspects

(•*•) Specimen: The specimen should co n sist of powder or s o lid

which i s s u f f ic ie n t ly fin e grained to give sharp, smooth d iffra c tio n l in e s .

In general, only a few milligrams o f specimen are required to obtain s a t is ­

factory r e s u lts . The optimum diameter of the specimen i s about 0,1mm.,

b u t^ iz e s up to 0 .3 mm. are sa tis fa c to r y . The specimen i s usually

rotated to increase the randomness o f orien ta tion .

Camera: A camera of nine centimetre diameter may be employed

fo r nearly a l l id e n tif ic a tio n work. There are various types of film

arrangement, the ones used in th is work being due to van Arkel (F ig .18),

and Straumanis-Ievins (F ig .19)*

( i i i ) Choice o f rad ia tion : The choice of radiation i s governed

by many fa c to rs . Among these are the avoidance of ex c itin g X-radiation

and the d e s ir a b ility of taking as many photographs as p ossib le with a

sin g le standard rad iation in order to sim plify the checking of d iffra c tio n

patterns against each other. The most commonly used rad iation being

copper K , which i s sa tis fa c to r y fo r a very wide range o f problems. ForCL

reasons which w il l be sta ted la te r (page 126) molybdenum K radiation ua.s

also used in the course of th is work. Since irra d ia tio n of these target

m aterials by X-rays covering a range of wavelengths produces as w ell

as white rad ia tion s, i t i s generally more convenient to work with a

f i l t e r e d radiation since the presence of r e f le c tio n s merely com plicates

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FIGUR

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-U 3 -

F 1 G U R E 18VAN ARK EL

F I G U R E 19STRAUMANIS-IEVINS

THE VARIOUS FILM ARRANGEMENTS USED IN DEBYE- SCHERRER CAMERAS AND THE KIND OF RECORD OBTAINED FROM EACH. THE DOTTED LINES JOIN CORRESPONDING POINTS ON THE ROLLED AND UNROLLED FILM.

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the d iffra c tio n patterns*

( iv ) Choice o f F i l t e r : The f i l t e r must co n sis t of a m aterial

having i t s K absorption edge at a wavelength between the K andct. pl in e s of the X-ray tube target element. Thus a n ick el f i l t e r i s

used fo r copper rad iation and a zirconium f i l t e r fo r molybdenum,

rad iation .

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EXPERIMENTAL

P recip ita tion Procedures

I t was decided to t r y and confirm some o f the re su lts of the early

papers and at the same time attempt to gain fresh information; accordingly

the experiments below were performed. These f a l l in to two groups,

namely j

(a) P rec ip ita tio n stu d ies with so lu tion s of constant thorium

concentration and variable barium concentration,

(b) Sim ilar stu d ies, but-w ith so lu tion s having variable 'thorium

concentration and constant barium concentration,

The experiments under sec tio n (a) can be further sub-divided :

( i ) Those in which a ca, M/30 stock so lu tion of thorium was used,

( i i ) Those in which a ca, M/lO stock so lu tion o f thorium was used,

w h ilst those under section (b) can be sub-divided thus :

( i ) Those in which 25 ml, of approximately M/lO so lu tion of barium

ch loride was used,

( i i ) Those in which 50 ml. of an approximately M/lO so lu tion o f

barium chloride was used.

The i n i t i a l strengths of a l l solu tions were determined prior to the

commencement of the experiments by the methods ind icated in the a n a ly tica l

sectio n .

Experiments with a constant thorium concentration. In the case o f the

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experiments requiring a constant thorium concentration and a variable

barium concentration, 100 ml. of 1M hydrochloric acid solution were taken

and to each sample 10 ml. of a oa. M/30 so lu tion of thorium chloride were

added by means of a p ip e tte . Then varying amounts, between 5 and 50 m l.,

o f an approximately Hi/ 10 so lu tion of barium chloride in 1M hydrochloric

acid were added from a burette. The barium was p recip ita ted as sulphate

by adding a s lig h t excess of about 1M sulphuric acid . The so lu tion was

therefore about 1M in hydrogen io n s . Two ser ies of experiments were

performed; the so lu tion s in one ser ie s were allowed to stand for twenty-

four hours and those in the other fo r seven days before f i l t r a t io n . At

the end of these periods the so lu tion was f i l t e r e d through a gooch

cru cib le(prev iously dried and weighed) and the p rec ip ita te was washed

rapidly with 1M hydrochloric acid . The f i l t r a t e and washings were com­

bined and analysed for thorium. From these figu res and the i n i t i a l data

i t was p ossib le to f in d (by d ifferen ce) the amount o f thorium lo s t from

so lu tio n . The p rec ip ita te was dried to constant weight in an oven at

110°C, From th is weight and the i n i t i a l data the excess amount of

p rec ip ita te over the th eo retica l could be found.

The second se r ie s again required a constant thorium concentration

and variable barium concentration. The experiments were performed in

an analagous fash ion to the above except that M/lO thorium chloride

stock so lu tion was used in place of M/30. T w o se r ie s were performed,

one standing fo r twenty-four hours and the other for seven days.

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Constant Barium. In these experiments 100 ml* of 1M hydrochloric acid

were taken as before, varying amounts (5“50 m l.) of M/30 thorium chloride

were added by means of a burette and 25 ml. ( b ( i ) ) or 50 ( b ( i i ) ) of barium

chloride in 1M hydrochloric acid were added by means of a p ip e tte . The

barium was then p recip ita ted as sulphate with sulphuric acid a s abv

The same procedure was follow ed from th is point and the required data

were obtained in a sim ilar way*

In both cases two ser ie s o f experiments were performed with standing

tim es, a fter p rec ip ita tio n , of twenty-four hours and seven days.

X-Ray Procedures.

A number o f X-ray powder patterns were taken of some of the pre­

c ip ita te s obtained above and a lso of barium and thorium sulphates pre­

c ip ita ted in the same way. The p rec ip ita tes ohosen fo r these stu d ies

are ind icated by arabic numerals in F ig .29* The Debye-Scherrer powder

method was used in a l l cases.

The p rec ip ita te s obtained were f in e ly powdered and a small portion

attached to a f in e g la ss f ib re (about 0.3 mm in diameter and about one

centim etre in length) by means of an acetate cement, fo r example,

durofix. This type o f cement being used in order to avoid contamination,

of the m aterial to be examined, with water from the more usual cements.

The specimens thus obtained were placed in the camera and accurately

centred. Two nine centimetre (diameter) cameras were used, one a Unicam,

made use of the van Arkel type mounting (page 113) and the other, a H ilger

used the Straumanis-Ievins mounting (page 113) •

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These specimens were then irrad iated w ith, in the m ajority of

cases, copper K radiation (1.54A), a n ick el f i l t e r being used to ensureCL

that th is was the only radiation obtained. The X-rays were produced by

means of a P h ilip s sea led -o ff tube run at 32 k ilo v o lts and 12 m illiam ps,

the exposure times being up to e igh t hours.

In the cases o f the experiments conducted with molybdenum

rad iation a zirconium f i l t e r was used and the X-rays were produced on a

Newton-Victor continuously evacuated se t run at about 40 k ilo v o lts and

15 m illiam ps.

During the course of the work i t was thought that atmospheric

moisture may have been taken up by the p rec ip ita tes w h ilst in the camera

and that th is may have had an e f fe c t on the d iffra c tio n patterns obtained.

Accordingly a few experiments were carried out with the m aterials under

examination sealed o ff from the atmosphere. This was aohieved by taking

some of the powder to be examined in a f in e hard g la ss ca p illa ry tube

(diameter 0 ,5 mm.) and sea lin g the ends in a small bunsen flame. The

specimen was then mounted in the camera and irrad iated as b efore.

Other Experiments:

( l ) Experiments were conducted to fin d the amount o f water taken up

from the atmosphere by the p rec ip ita te s and by the thorium and barium

sulphates. A small amount of the m aterial, approximately 0.25 g»> was

accurately weighed out on to a watch g la ss , and covered in such a way as

to allow free access of a ir , and at the same time, prevent dust from

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s e tt l in g on i t . After a time equal to the time of exposure in the X-ray

experiments (generally eigh t hours) the watch g la ss and p rec ip ita te were

re-weighed. Hence by subtraction the amount of water taken up could be

found.

(2) During the course of the X-ray experiments some doubt was cast

on the accuracy of the an a ly tica l resu lts obtained in the p rec ip ita tio n

experiments and as a check the fo llow ing experiments were performed :

(a) A small quantity of the p rec ip ita te was accurately weighed out

and transferred to a platinum crucib le together with about ten times i t s

bulk of sodium carbonate. The crucib le was then covered w ith a platinum

l id and was heated, gen tly at f i r s t , over a bunsen burner and la te r over

the f u l l strength of a meker burner. After about eigh t hours heating

over the meker burner the cru cib le , l id , and melt were allowed to cool

and then placed in a beaker o f d ilu te hydrochloric acid and warmed for

several hours on a steam bath. The crucib le and l i d were then removed

and washed with water, the washings being added to the hydrochloric acid

so lu tio n . This so lu tion was then evaporated to small bulk and analysed

for thorium and barium as in d icated in the an a ly tica l section .

(b) P rec ip ita tes were taken and a fter accurate weighing were

digested fo r several hours with concentrated hydrochloric acid; th is

leached out the thorium. The residual barium sulphate was f i l t e r e d o f f ,

the so lu tion evaporated nearly to dryness and the thorium determined

with EDTA.

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RESULTS AND DISCUSSION

The resu lts of these experiments are given in Tables 1 - 8 ,

the barium and thorium m olarities being ca lcu la ted from a knowledge o f

the amounts o f barium and thorium added. The *mole ratio* o f barium to

thorium was a lso calcu lated from these data. The th eo retica l weight

of barium sulphate p rec ip ita te was calcu lated from the amount of barium

added. The thorium lo s t from so lu tion ? as ca lcu lated from the t itr a t io n

figu res and expressed as amount of ^(SO^)^ lo s t from the so lu tion .

The re su lts are p lo tted in F igs. 20 to 29* F igs. 20 and 22 are

p lo ts of the excess weight of the p rec ip ita te against the th eo retica l

weight of barium sulphate and F ig s . 24 and 26 are p lo ts of the excess

weight against the number of cubic centim etres of thorium chloride

so lu tion added. An examination of these figu res shows th at, according

to the conditions of the experiment, the amount of p rec ip ita te i s some­

times greater a fter seven days standing than a fte r twenty-four hours

(F ig .20) and sometimes le s s a fter seven days (F igs. 22,24, and 26).

This i s in agreement with the work o f Balcar and Stegeman (82), and of

K olthoff (8 8 ). A p ossib le explanation of th is i s that part of the

barium i s re -d isso lv ed and replaced by thorium or that some of the

thorium r e -d isso lv e s on long standing. I t i s p ossib le that both of

these phenomena occur.

A further examination of these figu res shows that there are stages

at which the amount of excess weight of p recip ita te r is e s suddenly with the

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amount of barium or thorium added. This might suggest a change from one

type of p rec ip ita te to another. Accordingly the ra tio of Ba/Th in the pre** ]

c ip ita te was p lo tted against the ra tio of Ba/Th in the i n i t i a l so lu tion

(F ig .28), and i t appeared that the points f e l l in to four d is t in c t groups

( l - IV in the f ig u r e ) . The points in each group l i e w ithin a given r&nge

iiBarium concentration ||

0.020M - 0.035M

0.011)1 - 0.028M I

0.008M - 0.032M

0.008M - O.Oli+M

I t i s n oticeab le that the points in 111 are due to the whole range of

barium concentration ava ilab le , w h ilst 1, 11 and IV form d is t in c t groups.Ii

Furthermore, most of the poin ts in 111 are the r e su lts of 24 hours standing. |ii

This suggests that 111 might correspond to a metastable s ta te . Hence we j

might assume that there are three d is t in c t types o f p recip ita te ( l , 11, and |

IV) and an interm ediate stage 111.

With reference to Tables 4 - 11, in some cases the excess weight o f

p rec ip ita te over the th eo re tica l amount i s c lo se ly accounted fo r by the

amount o f thorium lo s t from so lu tion represented as Th(SO^)^. In other

cases increases in the weight of p rec ip ita te are le s s than the amount of »

thorium lo s t from so lu tion; th is would lead us to suggest that part of the

barium i s red isso lved and replaced by thorium. In further cases the amount

of thorium lo s t from so lu tio n represented as Th^O^)^, does not account

for the excess weight of p rec ip ita te ; i t might be supposed that in th is

case ThCsO^)^ i s p recip ita ted as an hydrate except that th is seems

of barium and thorium concentration thusThorium concentration

I . 0.002M

I I . 0.002M - 0.007M

I I I . 0.003M - 0.007M

IV. 0.007M

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to occur more often with so lu tion s containing a high overa ll e le c tr o ly te

concentration.

Further reference to F ig. 26 shows that the Ba/Th ra tio in the

p rec ip ita te appears to approach a ra tio of 2/1 with respect to the ra tio

of those two ions in so lu tio n .

These r e su lts would rule out the p o s s ib il ity of physical sorption

and might in fa ct in d icate that certa in ra tio s of Ba/Th in a sulphate

p recip ita te are preferred.

From F ig .28 i t can be seen that fo r p rec ip ita tes in Group IV

the ra tio i s of the order of 7 ! 1 , for p rec ip ita tes of Group 111 the

ra tio i s about 14 : 1* The preferred ra tio s therefore might be 7 : 1>

14 ; 1, 21 : 1, 28 j 1, (or % : 1, 15 s 1, 22§- : 1, 30 : l ) , but i t i s

d i f f ic u lt to assign p recise values.

From F igs. 21 and 23 i t would appear that the amount of thorium

lo s t from so lu tion r is e s rapid ly at f i r s t and then tends to le v e l o ff

and remain at a d efin ite value at higher concentrations of barium. This

i s in agreement with the work of Kammer and Silverman (81). F ig s. 23

and 27 are graphs of the amount of thorium lo s t from so lu tion against the

number o f cubic centim eters of thorium chloride added, these tend to r ise

throughout the range and i t i s a matter fo r conjecture as to whether

there would come a thorium concentration when they would le v e l o f f .

W hilst no quantitative data were taken on the rate of s e t t l in g

of the p r ec ip ita te s , i t was noticeab le in the experiments in which the

thorium concentration was the variab le , that the rate of s e t t l in g was

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-123-

dependent on the amount of thorium present. ^he observations were in

general agreement with those of Balcar and Stegeman (82).

The data for the ra tio Ba/Th used for F ig s . 28 and 29 were obtained

by taking the actual weight of p rec ip ita te and subtracting the thorium

lo s t from so lu tion ca lcu la ted as Th^SO^g, to give the weight of barium

sulphate, from which the amount of barium could be ca lcu lated .

X-Ray D iffraction Studies

The main object of these experiments was to attempt to fin d out

whether there was any change of c r y s ta l structure in the arbitary groups

of p rec ip ita tes ind icated e a r lie r .

Accordingly the p rec ip ita tes marked with arabic numerals in F ig .29

were obtained and subjected to X-rays in the manner already described.

In addition barium chloride so lu tion s in 1M hydrochloric acid were taken

and barium sulphate was p recip ita ted and dried as before. The barium

sulphate thus produced was then used to obtain a powder picture for re­

ference purposes. This p ictu re i s reproduced in F ig .30.

Powder P ictures

Of the p rec ip ita te s , the f i r s t X-ray powder p icture taken was that

of 'p rec ip ita te 1* which contained about 5 per cent thorium. An examina­

tio n of the pattern obtained showed only the pure barium sulphate pattern .

'P recip ita te 2* was then taken and the powder picture again showed no

signs of any change from that of barium sulphate. This p rec ip ita te

contained roughly 7 per cent thorium.

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Powder p ictures were then taken of a l l the p rec ip ita tes indicated

and even when the amount of thorium present was as high at 20 per cent

the only change observed in the pattern was a s lig h t d iffu seness of

certa in of the l in e s . Sample patterns are to be seen in F igs. 33 &nd 34*

I t i s worthy of note th at, in general, amounts as low at 3 P©r cent of

another compound or element can be detected by the method employed here,

provided th e ir structures are d ifferen t (94)> but in some cases as much as

lOfo of the ’fo r e ig n 1 substance i s required (94)*

Chemical A nalysis of P recip ita tes

The fa c t th at the thorium in the p rec ip ita te did not appear to be

shown in the pattern led to the chemical an alysis of the p rec ip ita te s ,

th is being carried out in the manner already described (page HSJ). The

r e su lts were in c lo se agreement with those found previously . This agree­

ment supplied confirm ation of the e a r lie r r e su lts and showed beyond doubt

the presence of thorium in the p rec ip ita te s .

At th is stage i t was decided to tr y to obtain a sample of thorium

sulphate p recip ita ted in the same way as the m ixtures. However, the

thorium sulphate remained in so lu tion un less a very large excess of su l­

phuric acid was added to the so lu tion of thorium chloride in 1M hydro-

chlorio acid . N evertheless th is p rec ip ita te was obtained and washed and

dried as before. W hilst i t i s im possible to say whether th is p rec ip ita te

has the same composition as the thorium compound carried down with the

barium sulphate, i t was judged worthy o f further in v e stig a tio n .

This p rec ip ita te was subjected to the Debye-Scherrer method as before

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-125-

and the pattern obtained can be seen in F ig ,32. I t corresponds with

that o f Th(S04 )2,4H20. As can be seen th is pattern i s very sim ilar to

that of the barium sulphate.

As a re su lt of th is in v estig a tio n the Ba/Th ra tio s in the p rec ip ita te s ■

were re-ca lcu la ted on the b asis the thorium being carried down as

Th(S0^)2 .4H20. I t was found that the d ifference made by taking th is

figure was n e g lig ib le , making a d ifferen ce , in general, of the order o f

1 per cent, which made no appreciable a ltera tio n to the points on the

graph in F ig .29.

Experiments with Physical Mixtures j

Barium sulphate was mixed, in various proportions, With the thorium

sulphate that had been previously obtained. These physical mixtures

were then subjected to X-rays. Two of the patterns obtained are r e -Is

produced in Figs . 31 and 35- Fig * 35 i s the pattern of a mixture con­

tain ing about 16 per cent of the thorium compound, w h ilst th at of F ig .31

i s of a mixture containing 50 per cent of the thorium compound.

An examination of F igs. 30 and 32 shows that the barium and thorium

patterns are very sim ilar. This s im ila r ity of the lin e s i s due rather

to th e ir p o sitio n than th e ir in te n s i t ie s . Further evidence of th is

s im ila r ity i s provided by Table 9* This tab le was obtained by taking .

the barium sulphate pov^der pattern and find ing the !d* values of the most

in tense l in e s and assigning to these in te n s ity values on an arbitrary

scale of ten . A sim ilar procedure was adopted with the thorium sulphate

pattern . Reference to th is tab le shows that fo r every lin e on the

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- 126-

thorium sulphate pattern there i s a corresponding or nearly corresponding

lin e on the barium sulphate pattern . G-enerally, the l in e s have d ifferen t j!

in te n s it ie s but th e ir p o sitio n s aro almost exactly s im ilar . This c lo se

s im ila r ity should ( in physical mixtures) r e su lt in an in te n s if ic a t io n o f )

some of the barium l in e s , i . e . , those which correspond exactly and a

d iffu sen ess in those in which there i s a s lig h t d ifference in !d’ va lu e. ]i

F ig .31 which i s the pattern obtained from a 1 : 1 mixture of the two j

compounds shows that the only detectable d ifference i s a d iffu seness of

many of the lin e s due to th is overlapping. F ig .35 shows no change from

the pure barium sulphate pattern and in fa c t i t i s only with mixtures ]

containing about 40 per cent thorium sulphate that the s lig h t d iffuseness

exhib ited in F ig . 31 begins to appear.

.enum

Up to th is stage a l l the X-ray experiments had been conducted with j

copper K rad ia tion . This rad iation i s scattered almost equally by the jCL |

barium and thorium atoms so i t was decided, in view of the foregoing, to \\j

conduct experiments using molybdenum rad iation which i s scattered

almost twice as strongly by the thorium as by the barium. I t was hoped

from these experiments to be able to in te n s ify certa in of th e weaker thorium

l in e s and perhaps gain inform ation from the in te n s it ie s of the l in e s as

w ell as th e ir p o sitio n . I t i s unfortunate, however, that the molybdenum

radiation cramps the l in e s to the high angle region of the pattern and so

i t proved im possible to elu cid ate any information from the pattern obtained.

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-127-

Uptake of Water

With regard to the s lig h t d iffuseness found in ea r lier p ictures

(page 126), i t was o r ig in a lly thought that th is may be due to v/ater being

taken up from the atmosphere. The experiments already mentioned (page 118)

were carried out and i t was found that in the period of e ight hours that

the m aterials were open to the atmosphere, the amount of water taken up

was approximately 3 P©r cent by weight. I t was thought that th is would !

not a f fe c t the pattern obtained but as a check thorium sulphate was

irrad ia ted in a sealed tube and the pattern so obtained (F ig . 36) was com­

pared with that found in the normal way. As expected the two patterns

were id e n t ic a l .

Further Discussion

As can be seen from the work discussed above, i t i s d i f f ic u lt to draw

any f in a l conclusions but certa in fa c t do emerge. These are :~

( i ) The Debye-Scherrer powrder patterns of the barium and thorium

s a lt s as p recip ita ted are generally sim ilar, but whether the thorium s a lt

p recip itated separately i s the same as that p recip ita ted in the mixtures

i s open to some doubt.

( i i ) The c r y s ta llin e structures of th e mixtures are the same in the

four groupings suggested.

( i i i ) The p rec ip ita tes obtained from p recip ita tion of the mixtures

c le a r ly show a barium sulphate type structure, and th is would tend to rule

out the p o s s ib il ity of the formation of complex compounds unless they had

barium sulphate stru ctu res.

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•128-

( iv ) I t i s possib le that the compounds obtained are barium sulphate

cry sta ls with an overgrowth of thorium sulphate. Mixed c r y sta ls of th is

type are known, e .g . when one of the members i s in so lu b le , the soluble

compound can deposit o ry sta ls from so lu tion which are orientated in con­

form ity with the structure of th e insolub le compound. These are known

as orientated overgrowths, an example being calcium carbonate and sodium

n itra te (95 ). This may in fa c t be the case here although the re la tiv e

s iz e s of the ions involved are outside the range normally considered

conducive to th is type of c r y s ta l formation. In general i t seems

unlikely that complex s a lt s , such as, fo r example, BaJrh(SO^) 31 are

formed.

Summary »

To summarize,the thorium p recip ita ted from the mixtures of barium

' and thorium ch lorides could be (a) mainly Th^O^^.-^^O in which case

there would be no change in the pattern, (b) an overgrowth of the type

mentioned above. Again th is would show no change from the pattern o f

the barium sulphate•

At the present stage i t should be borne in mind that the above

are only suggestions, the evidence being in su ff ic ie n t to e s ta b lis h , beyond

a l l reasonable doubt, the above conclusions.

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-129-

T A B U L A R R E S U L T S F O R P A R T II

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-138-

* d* values and in te n s it ie s fo r the barium and thorium

sulphate patterns

Barium sulphate Thorium sulphate

d I d I

1.43 2 1.76 2

1 .54 2 1.86 2

1.68 2 2.12 2

1.76 2 2.23 2

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2.12 10 2.71 2

2.22 2 3.10 1

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9 .4 1

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FIGURE 3 0 .

BARIUM SULPHATE. VAN ARKEL MOUNTING.

FIGURE 3 1 .

PHYSICAL MIXTURE. 50% EACH OF THORIUM

AND BARIUM SULPHATES STRAUMANIS- IEVINS

MOUNTING.

FIGURE 32 .

THORIUM SULPHATE. VAN ARKEL MOUNTING.

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149 .

FIGURE 33 .

'PRECIPITATE 3 ’

( s ee page 1 2 4 ) .

THIS CONTAINED ABOUT 5$ THORIUM.

VAN ARKEL MOUNTING.

FIGURE 3 4 .

'PRECIPITATE 1 0 '

( s ee page 1 2 4 ) .

THIS CONTAINED ABOUT 20/3 THORIUM.

VAN ARKEL MOUNTING.

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FIGURE 35.

PHYSICAL MIXTURE OF THORIUM

and barium s u l p h a t e s .

CONTAINING 16% THORIUM SULPHATE.

VAN ARKSL MOUNTING.

FIGURE 3 6 .

THORIUM SULPHATE IN A SEALED TUBE.

VAN ARKEL MOUNTING.

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-151-

P A R T III

SUMMARY OF CONCLUSIONS

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-152-

As was expected the experiments with perchloric acid shov/ed very

l i t t l e evidence o f complex formation with thorium. The cation exchange

experiments may be in d ica tiv e of a s lig h t amount of complex formation or

merely the formation of a thorium perchlorate so lu tion by exchange of

hydrogen ions with thorium ions from the resin#

In agreement with the work of Kraus and Moore (60) and of Hyde ( 6l ) ,

thorium was found to show l i t t l e or no tendency to anionic complex

formation in hydrochloric acid and sodium chloride media# In the ca tion -

exchange experiments with hydrochloric acid, hov/ever, r e la t iv e ly large

amounts o f thorium were removed from cation exchangers in the thorium form#

These r e su lts may ind icate the formation of cation ic complexes, such as

ThCl , or of neutral IbCl^ or, more probably, a mixture of both. The

fa c t that thorium can e a s ily be displaced from a ca tion ic exchanger by 2M

hydrochloric acid i s in contradiction to the observation o f Hyde (6l ) that

thorium i s only removed when 5M (or stronger) hydrochloric acid so lu tion s

are employed.

The fa c t that the removal of thorium from a cation exchange resin by

means of sulphuric acid shows evidence of decreasing with increasing acid

concentration, w h ilst the sorption o f thorium an to an anion exchanger

appears to increase with increasing acid concentration, i s paradoxical.

This might lead to the conclusion that the graph in F ig . 12 would r is e to

a peak and then f a l l o f f rapidly. However, there i s evidence for the

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-153-

formation of anionic thorium sulphate complexes*

The disagreement in the lite r a tu r e (61, 62, 65, 66) with regard to

the thorium complexes present in n itr ic acid has been somewhat c la r if ie d .

There i s good evidence fo r anionic complex formation in n itra te media

and p a rticu la r ly in 8M n itr ic acid . The predominant complex may be

Th(N03) g=.

The r e su lts obtained with phosphoric acid and the thorium form of

ZeoKarb 225 show considerable complex formation, w h ilst the uptake of

thorium on to the anion exchanger DeAcidite FF from thorium-phosphate

so lu tion s i s sm all. This would lead to the conclusion that a mixture of

complexes i s formed (o f which some only are sorbed).

A few experiments were performed with arsenic acid so lu tion s and these

in d icate that in general the degree of complex formation i s high, probably

ly in g somewhere between that for sulphuric and that fo r phosphoric acid .

The co -p recip ita tion experiments were conducted in hydrochloric acid

so lu tion . I t i s possib le th at the thorium p recip ita ted from the mixtures

of barium and thorium chlorides could be e ith er mainly Tl^SO^g.^gO or an

overgrowth of the type mentioned previously (page no.128). In e ith er case

the X-ray d iffra c tio n pattern obtained would show no change from the

pattern of the barium sulphate.

I t i s u n lik ely that complex s a lt s of the type Ba ■Th(SO^)^1L

formed.

are

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-154-

B I B L I O & R A P H Y

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-155-

Thompson, J.R oy.A gric.Soc., 1850, 11, 68,

Way, J.R oy.A grio.Soc., 1850, 11, 315; 1852, 12, 123,

Gans, J& hrb.kgl.preusse.geol. Landesanstalt, 1905, 26, 179; 1906,22, 63.

Gans, Centr.M ineral.Geol., 1913, 22, 728.

Gans, German P at., 197,111 (1906); U.S.P&ts., 914,405 (1909);

943,555 (1909); 1,131,503 (1915).

Adams and Holmes, J.Soc .Chem.Ind., 1935, 24;, 11*

Griessbach, Ver« deut. Chemiker B eihefte, 1939, 31,, 1;

Angew.Chem., 1939, £2, 215*

Geunther-Schulze, Z.Electrochem., 1922., 28, 89 and 387#

Gustavson, J.Am.Leather Chemists’ A ssoc., 1924, 19, 446.

Gustavson, Ind.Eug.Chem,, 1925, 17. 577*

Schubert and Richter, J.Amer.ChGm.Soc,, 1952, Jkj 3529#

Schubert and Richter, J.Amer.Chem.Soo., 1954, 76, 3442.

Salmon, J . Chem.Soc., 1953, 2644#

Jameson and Salmon, J.Chem.Soc., 1955, 3&0.

Elson, The Actinide Elements, McGraw H ill (pub lishers), 1954, p .110.

S treet and Seaborg, J.Amer.Chem.Soc., 1950, 72, 2790.

Wish, Freiburg and Binney, J.Amer.Chem.Soc., 1954, 3444.

Thompson, Cunningham and Seaborg, J.Amer.Chem.Soo., 1950, 72, 2798.

King and Dismukes, J.Amer.Chem.Soo., 1952, 2 i , 1674*

Gustavson, Svensk Kern. T id ., 1946, £8, 2.

Gustavson,J.Soc.Leather Trades Chemists, 1951, 35. 160.

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-156-

(22) Gustavson, Svensk Kern.Ti&., 1951, £3, 167.

(23) Theis and Thorstensen, J. Intern, Soc, Leather Trades Chemists, 1947*

2±> 12^

(2i+-) Serfass, Theis, Thorstensen and Argarwal, J.Am.Leather Chemists’

A ssoc., 1948, L£, 132.

( 25) Salmon, Rev. Pure and Appl.Chem., 1956, 6, 24*

( 26) Schubert, R u sse ll and Myers, J.B iol.C hem ., 1950, 185« VM 00 •

( 27) Schubert, J.Phys.Chem ., 1952, J56, 113#

(28) Schubert and Lindenbaum, J.Amer.Chem.Soc,, 1952, 74% 3529.

(29) Jameson and Salmon, J,Chem .Soc,, 1954, 4013*

(30) L is te r and McDonald, J.Chem.Soc,, 1952, 4315%

(31) D’A le lio , U .S .P a t., 2,366,007 (1944).

(32) Pepper, J, Appl.Chem., 1951* 1, 124.

(33) H ohenstein and Mark, J .P o ly m .S c i. , 1946, 1, 127.

(34) Winslow and Matreyek, In d .Eng.Chem., 1951* 4*5* 1108,

(35) M ellor, T re a tise on Inorganic and T h eo re tica l Chem., V o l.9, pp.757-766

(36) Friedlieim and Szamatolsky, B er,, 1890, 1530.

(37) Reichenberg, Pepper and McAnley, J,Chem.Soc., 1951* 493*

(38) Gregor, J.Amer. Ciaem. S o c . , 1951* Zl*

(39) Samuelson, Svensk Kem.Tid., 1942, ^4, 170.

(40) Samuelson, Diss.Tekn.Hogsholan, Stockholm, 1944.

< u > Boyd, Adamson and Myers, J.Amer.Chem.Soo., 1947, 69, 2818,

(42) Bow Chemical Co., B r i t .P a t . , 683, 400 (1952).

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-157-

Hawdon, Linstead and Thomas, B rit.P at.A p p ln ., 7732/50.

The Permutit Co.Ltd., B r it .P a t., 694,778 (1953).

Rohm and Haas Co., B r it .P a t., 670,348 (.1952).

Dow Chemical Co., B r it .P a t., 679,853 (1952).

Winters and Kumin, Ind.Eng,Chem,, 1949, 41, 460.

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