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2. The Thermal Conductivity Detector (TCD) - Eawag-Empa Library

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<strong>2.</strong> <strong>The</strong> <strong>The</strong>rmal <strong>Conductivity</strong> <strong>Detector</strong> (<strong>TCD</strong>)<br />

<strong>2.</strong>1 DETECTION MECHANISM<br />

<strong>The</strong> thermal conductivity detector is among the most commonly used measuring<br />

devices in gas chromatography for monitoring substances separated in the column.<br />

This detector measures changes in the thermal conductivity of the carrier gas, caused<br />

by the presence of the eluted substances.<br />

<strong>The</strong> thermal conductivity, If, of component S is determined by the gas density, e,<br />

the mean molecular velocity, ij, the mean free path, 2, and the specific heat at constant<br />

volume, Cv:<br />

It follows from equation (<strong>2.</strong>1) that the thermal conductivity is a function of the size<br />

of the molecules, their mass and the temperature, as<br />

where D is the diffusion coefficient. <strong>The</strong> dependence of the thermal conductivity on<br />

the molecular masses of substances S and C is given by the relationship<br />

<strong>The</strong>rmal conductivity values for some compounds are given in Table <strong>2.</strong>1.<br />

<strong>The</strong> thermal conductivity of binary mixtures is given by the thermal conductivities<br />

of the components and their molar fractions, x [46]:<br />

where A and B are constants and .yS = 1 - sc.<br />

By solving equation (<strong>2.</strong>4) for a change in the conductivity of a binary mixture [22],<br />

an expression that quantitatively describes the non-linear variation of the conductivity


40<br />

with the concentration is obtained (see Fig. <strong>2.</strong>1)<br />

TABLE <strong>2.</strong>1<br />

THE THERMAL CONDUCTIVITY OF SOME COMPOUNDS<br />

w N<br />

Compound KS x lo3 [W/cm. K] Compound KS x lo3 [W/cm. K]<br />

1710<br />

1470<br />

303<br />

240<br />

239<br />

24s<br />

23 I<br />

216<br />

164<br />

7 0<br />

FIG. <strong>2.</strong>1. <strong>The</strong>rmal conductivities of some binary mixtures.<br />

145<br />

86.2<br />

154<br />

173<br />

152<br />

111<br />

190<br />

170<br />

For very low concentrations of the eluted substance, all the terms in the expanded<br />

Taylor series (equation (<strong>2.</strong>5)) can be neglected except for the first, thus giving a linear<br />

relationship between the concentration of the eluted substance and the change in the<br />

conductivity of the binary system.<br />

Measurement with the <strong>TCD</strong> is based on monitoring changes in the electric con-<br />

ductivity of the filament, caused by variations in its temperature during passage of


the gaseous mixture through the measuring cell. A temperature gradient is established<br />

due to transfer of thermal energy by the medium. Under stationary conditions, the<br />

amount of heat transferred, Q, is proportional to the thermal conductivity of the<br />

flowing gaseous mixture and to the difference in the temperatures of the filament, T,,<br />

and the cell walls, T,:<br />

During the design of practical measuring devices, it was found that the overall<br />

amount of heat transferred is not given by the thermal conductivity of the medium<br />

alone, but that the molar heat capacity and other factors also play a role. <strong>The</strong> follow-<br />

ing processes contribute to the overall heat change, i.e., to the measured signal:<br />

- the thermal conductivity of the medium;<br />

- forced convection of the gaseous mixture;<br />

- free convection and diffusion of the gas;<br />

- the thermal conductivity of leads and connections;<br />

- thermal radiation.<br />

<strong>The</strong> participation of the thermal conductivity and of forced convection of the gas<br />

in the overall heat transfer can be distinguished only with great difficulty. Forced<br />

convection represents heat transfer coupled with mass transport under the dynamic<br />

conditions present in the gas chromatograph and amounts to about 25% of the<br />

overall change. This part of the transferred heat is proportional to the volume velocity<br />

of the gas, u, and to its heat capacity, C,:<br />

Hence the <strong>TCD</strong> signal depends on the flow-rate of the carrier gas.<br />

<strong>The</strong> contribution of free convection corresponds to energy transfer in the concen-<br />

tration gradient and is negligible compared with the other factors.<br />

Heat transfer by the leads and electrical connections is determined by their cross-<br />

section, length and thermal conductivity. <strong>The</strong>refore, it is desirable that the leads to<br />

the sensor should be as short as possible and have as small a cross-section as possible.<br />

It has been found that this parameter does not have a large influence on the overall<br />

change in the <strong>TCD</strong> signal in devices with heated filements, but that its importance<br />

increases when thermistors and transistors are used as sensors:<br />

Heat radiation depends on the surface area of the measuring element, on its<br />

temperature and on its material quality. <strong>The</strong> literature gives values of less than 4%<br />

for the contribution of thermal radiation to the overall heat transfer.<br />

41


42<br />

<strong>2.</strong>2 <strong>TCD</strong> SIGNAL<br />

Measurement with the thermal conductivity detector is based on monitoring changes<br />

in the resistance of the sensor, R,. A current I passes through the sensor and the<br />

thermal equilibrium in the measuring cell, through which a gaseous mixture with<br />

a thermal conductivity of K passes, can be expressed by the equation<br />

12Rf = J d(T, - T,)<br />

where a is the geometric constant of the measuring cell and J is Joule’s constant.<br />

It follows from the experimental arrangement that part of the thermal energy is lost<br />

during the passage of the gaseous mixture through the measuring cell and is manifested<br />

by a decrease in the sensor temperature, T,, as the temperature of the cell walls, T,,<br />

can be considered to be constant because of their high heat capacity. <strong>The</strong> sensor<br />

resistance is a linear function of the temperature:<br />

R, = RP(1 + XT,)<br />

(<strong>2.</strong>10)<br />

and therefore the measured changes in the resistance are given by the relationships<br />

and<br />

AR, = aRP. AT,<br />

AK<br />

AT, = - (T, - T,)<br />

K<br />

(<strong>2.</strong>11)<br />

(<strong>2.</strong>12)<br />

<strong>The</strong> signal of the thermal conductivity detector, SrcD, is proportional to the change<br />

in the voltage of the measuring bridge, AE:<br />

srcD N AE -f --<br />

AR<br />

- AR a(T, - T,)<br />

(<strong>2.</strong>13)<br />

R, K (1 + aT,)<br />

From equation (<strong>2.</strong>13) it follows that the signal depends on a number of parameters,<br />

the most important being<br />

- the voltage of the measuring bridge, E;<br />

- the geometric constant of the measuring cell, a;<br />

- the properties of the construction material, expressed by a;<br />

- the temperatures of the sensor and the cell walls, T, and T‘, respectively;<br />

- the thermal conductivity of the carrier gas, gc, and its flow-rate;<br />

- the thermal conductivity of the eluted substance, AK.<br />

As has already been mentioned, the <strong>TCD</strong> signal is not given by changes in the<br />

thermal conductivity of the gaseous mixture alone; forced convection of the material,<br />

which has a certain heat capacity, is also important. It is obvious that this contribu-


tion will become smaller with increasing participation of diffusion in the mass trans-<br />

port in the measuring cell. <strong>The</strong>refore, the term containing heat capacities is most<br />

significant with flow-through cells. Bearing this in mind, the following expression has<br />

been derived for SJCD [28, 291:<br />

43<br />

(<strong>2.</strong>14)<br />

where constants A and 6 are determined by the effective collision cross-sections and<br />

by the molecular weights of the eluted substances and of the carrier gas, where<br />

0 < A < 1 < 6, and u, is the molar flow-rate.<br />

<strong>The</strong> signal of the thermal conductivity detector is therefore strongly dependent on<br />

the molecular weights of the eluted substance and the carrier gas. It generally holds<br />

that the thermal conductivity decreases with increasing molecular weight, whereas<br />

the heat capacity increases. If hydrogen is the carrier gas, then all eluted substances<br />

will have lower thermal conductivities and higher heat capacities. <strong>The</strong> difference in<br />

the thermal conductivity term in the proportionality (<strong>2.</strong>14) increases with increasing<br />

molecular weight of the eluted substance and is always negative; the difference in the<br />

thermal capacity term increases and is positive. Hence the two processes have opposite<br />

effects and under certain circumstances their sum is equal to zero.<br />

<strong>2.</strong><strong>2.</strong>1 <strong>TCD</strong> background current<br />

<strong>The</strong> background current of the thermal conductivity detector is given by the compo-<br />

sition of the carrier gas, by its flow rate and by the detector temperature. As all<br />

practical designs employ a compensation bridge circuit, it is pointless to specify<br />

background current values. <strong>The</strong> <strong>TCD</strong> noise is caused by fluctuations in the detector<br />

temperature and in the carrier gas flow-rate [12]. For this reason, the measuring and<br />

the reference branches of the thermal conductivity detector are usually connected in<br />

a bridge circuit. This circuit is indispensable with flow-through and semi-diffusion<br />

cells, while diffusion cells yield results that are independent of the flow-rate and thus<br />

they have the lowest noise level.<br />

<strong>2.</strong><strong>2.</strong>2 <strong>TCD</strong> response<br />

<strong>The</strong> <strong>TCD</strong> response is the sum of the signals, SJCD, over the substance elution time.<br />

It follows from equations (<strong>2.</strong>13) and (<strong>2.</strong>14) that the relative magnitude of the signal<br />

depends on the character of the eluted substance; it decreases with increasing mo-<br />

lecular weight. A criterion frequently applied during evaluation of the effect of the<br />

structure of the eluted substance on the signal of the thermal conductivity detector<br />

is the relative molar response (RMR) [2, 3, 471. <strong>The</strong> RMR values are proportional<br />

to the various measuring sensitivities for various substances caused by their different


44<br />

thermal conductivites. <strong>The</strong> literature gives the dependences of S<strong>TCD</strong> on the molar and<br />

weight percent content of a substance. When light carrier gases are employed, then<br />

the proportionality of the signal to the weight per cent of the substance is usually<br />

TABLE <strong>2.</strong>2<br />

THE RELATIVE MOLAR RESPONSE TO ORGANIC OXYGEN-CONTAINING<br />

COMPOUNDS AND TO ALKYL-AROMATIC HYDROCARBONS [16]<br />

M - molecular weight<br />

Organic compounds<br />

Number of carbon<br />

atoms<br />

Equation for RMR<br />

n-Alkyl-aromatic c6-c10 0.741.M + 17.0<br />

hydrocarbons<br />

Primary alcohols c1-c4 0.67<strong>2.</strong>M + 25.4<br />

Esters RCOOR’<br />

Methyl ketones<br />

R = Co-C,;<br />

R’ = Ci-C4<br />

C,-C2<br />

0.630.M + 25.9<br />

0.688.M + 24.6<br />

n-Aldehydes<br />

n-Ethers<br />

c1-c6<br />

c2-c4<br />

0.631.M+ 21.9<br />

0.473.M + 49.5<br />

used. In any event, the use of relative responses is to be recommended for quantitative<br />

measurements, as they depend very little on experimental conditions such as the<br />

bridge voltage, cell temperature and flow-rate. <strong>The</strong> RMR values for homologous<br />

FIG. <strong>2.</strong><strong>2.</strong> <strong>The</strong> concentration dependence of the <strong>TCD</strong> response to some hydrocarbons,<br />

N, - carrier gas, 1 - pentane, 2 - heptane, 3 - octane [29].<br />

series of hydrocarbons, alcohols, etc., are given in Table <strong>2.</strong>2 [16]. <strong>The</strong>se values are<br />

obtained using hydrogen as the carrier gas and only a narrow range of molecular<br />

masses is covered. When the values are compared with those given in the literature


[25, 341, substantial differences are found. <strong>The</strong> validity of the published relative re-<br />

sponse rates must be judged carefully, as data concerning the measuring cell geometry<br />

and the experimental conditions are sometimes not specified. RMR values differing<br />

by as much as 18% between flow-through and semi-diffusion cells have been found<br />

[40]. It should be emphasized that, when using nitrogen as the carrier gas, even the<br />

significance of empirical RMR values is doubtful. Under these conditions, direct<br />

calculation of the concentration from the temperature dependences of il in the<br />

carrier gas employed [SO] has only limited validity.<br />

<strong>The</strong> molecular weight of the eluted substance significantly affects the character and<br />

magnitude of the JCD response. As the thermal conductivity decreases with increasing<br />

molecular weight, while the heat capacity increases, these two parameters have oppo-<br />

site effects and lead to conversion of negative peaks into positive peaks. This conver-<br />

sion is important with high-molecular-weight carrier gases, e.g., nitrogen. Fig. <strong>2.</strong>2<br />

shows that the change in the signal polarity is attained earlier with increasing mole-<br />

cular weight.<br />

TABLE <strong>2.</strong>3<br />

PARAMETERS CHARACTERIZING THE THERMAL CONDUCTIVITY<br />

DETECTOR WITH VARIOUS SENSORS<br />

Parameters ~.<br />

Sensor<br />

heated filament thermistor transistor<br />

Sensitivity [mV/mole] 4 x 104 4 x 105 <strong>2.</strong>5 x 106<br />

Linear dynamic range 5 4.4<br />

Noise [pV]<br />

<strong>The</strong> lower detectable amount<br />

f 3 [I1 & 10 56<br />

[PPnlI<br />

Proportionality constant<br />

5 0.2 0.012<br />

ImVIKI 6 2900<br />

<strong>The</strong> basic parameters of the thermal conductivity detector depend on the exper-<br />

imental conditions used and therefore they are discussed in greater detail in the<br />

following paragraphs. Generally, it can be stated that the thermal conductivity<br />

detector is a universal measuring device with a wide linear dynamic range. However,<br />

the minimum detectable amounts are sometimes large and then other detectors are<br />

preferable. Some parameters characterizing the thermal conductivity detector are<br />

listed in Table <strong>2.</strong>3. <strong>The</strong> linearity and linear dynamic range must be given in log-log<br />

coordinates because of the exponential form of equation (1.23).<br />

45


46<br />

<strong>2.</strong>3 EFFECT OF EXPERIMENTAL PARAMETERS<br />

ON THE MAGNITUDE AND SHAPE OF THE <strong>TCD</strong> SIGNAL<br />

<strong>2.</strong>3.1 Carrier gas<br />

In measurements with the thermal conductivity detector, hydrogen, helium, nitrogen,<br />

argon [45], carbon dioxide and mixtures of various gases, e.g., air or nitrogen with<br />

5-10% of hydrogen or helium [43], are employed as carrier gases. <strong>The</strong> suitability<br />

of various carrier gases can be evaluated with reference to the discussion related to<br />

equation (<strong>2.</strong>14).<br />

If hydrogen or helium is used as the carrier gas, the difference in the thermal<br />

conductivities is always large and always negative. When the eluted substance is an<br />

inert gas with a low molecular weight, then the term containing the heat capacities<br />

plays almost no role and the <strong>TCD</strong> value is given chiefly by the change in the thermal<br />

conductivity of the gaseous mixture.<br />

When nitrogen is used as the carrier gas, the changes in the conductivity caused by<br />

the presence of an eluted substance are small, but the difference in the heat capacities<br />

increases significantly. It is evident that the magnitude of the <strong>TCD</strong> signal is inversely<br />

proportional to the molecular weight of the eluted substance and generally SL, is<br />

greater than SLY, as the thermal conductivity and heat capacity terms in equation<br />

(<strong>2.</strong>14) are comparable for nitrogen.<br />

<strong>The</strong> purity of the carrier gas effects the magnitude of the <strong>TCD</strong> signal [20]. If<br />

a sample is injected into a carrier gas containing impurities, then, owing to changes<br />

in the partial pressures, the impurities are replaced by the eluted substance and the<br />

resulting change in the signal is small. For this reason, pure carrier gases should be<br />

employed, although identical sensitivities for measurement with pure and impure<br />

carrier gases have sometimes been reported [45].<br />

<strong>The</strong> pronounced dependence of the signal of the thermal conductivity detector on<br />

the gas flow-rate follows from the detection mechanism, involving removal of heat<br />

by forced convection of gases in the measuring cell. As already mentioned, this<br />

effect decreases with increasing participation of diffusion processes in the measuring<br />

cell; the dependence of the <strong>TCD</strong> signal on the flow-rate is negligible with the diffusion<br />

type of cell, expecially when a light carrier gas is employed [38]. It follows from<br />

equation (<strong>2.</strong>14) that the thermal conductivity term is independent of the flow-rate.<br />

<strong>The</strong> change in the signal with increasing flow-rate will be greater the greater is the<br />

(CP, - CP~) value, i.e., the greater is the molecular weight of the eluted substance.<br />

This change, leading to peak inversion, will naturally be greater and more frequent<br />

when nitrogen is used as a carrier gas because of the similarity of the conductivity<br />

and heat capacity terms in equation (<strong>2.</strong>14).<br />

A decrease in the signal is not always observed during a change in the carrier gas<br />

flow-rate; in fact, over a certain range of flow-rates, there is virtually no signal change.<br />

This is due to the fact that the elution peak becomes narrower with increasing flow-


ate and hence the fdet/d t ratio increases with increasing detector volume. Consequently,<br />

the mean concentration of the eluted substance in the effective volume of<br />

the detector increases and a maximum concentration is attained.<br />

<strong>The</strong> dependence of the response on the flow-rate, which is regulated either before<br />

or after the column, is depicted in Fig. <strong>2.</strong>3, from which it follows that the two<br />

dependences have the same shapes, i.e., the products of Cs and of the integration time<br />

are identical.<br />

t<br />

t ' I-<br />

I<br />

FIG. 1.3. <strong>The</strong> dependence of the JCD response on the flow-rate of the gaseous mixture;<br />

A - flow-rate varied before the column, B - flow-rate varied after the column, before<br />

the detector inlet [18].<br />

From these dependences, it follows that the type of carrier gas used is of basicimpor-<br />

tance. It is advisable to avoid the use of nitrogen and to work with hydrogen or helium.<br />

When using heavier carrier gases, the relationship between the response and the concen-<br />

tration may be markedly non-linear in the region of chromatographically significant<br />

concentrations, resulting in distortion and inversion of chromatographic peaks.<br />

<strong>2.</strong>3.2 Construction of the JCD<br />

<strong>The</strong> measurement of thermal conductivity is carried out with a sensor, the resistance<br />

of which is strongly dependent on the temperature of the medium (Fig. <strong>2.</strong>4). <strong>The</strong><br />

sensor itself is at a temperature 7;, which is higher than the temperature of the walls<br />

47


48<br />

of the measuring cell T,. <strong>The</strong> sensor temperature is constant with stationary heating<br />

conditions and a constant flow-rate of an unchanging gaseous mixture. A change in<br />

the composition of the flowing gases is reflected in a change in the sensor temperature,<br />

causing a change in the sensor resistance, R,, thus providing an electrically treatable<br />

signal. At present, heated filaments, thermistors and transistors are employed as<br />

sensors.<br />

FIG. <strong>2.</strong>4. <strong>The</strong> dependence of the sensor resistance on temperature; a - heated filament,<br />

b - thermistor, c - transistor.<br />

<strong>The</strong> heated filament was the first sensor to be used in the thermal conductivity<br />

detector. <strong>The</strong> dependence of its resistance on temperature is linear over wide temperature<br />

range (up to 400" C). This advantage is partly offset by its relatively low<br />

sensitivity to temperature changes (see Table <strong>2.</strong>3.).<br />

In addition to heated filaments, thermistors with negative thermal coefficients are<br />

used as sensors. <strong>The</strong> thermistor resistance is an exponential function of temperature<br />

and the maximum temperature used is about 100 "C; above this value, the sensitivity<br />

of the thermistor towards ,temperature changes is very low. If the thermistor resistance<br />

equals RP at a particular standard temperature, To, (usually 25 'C), then the resistance<br />

at temperature T, is given by the relationship.<br />

R, = RP exp [ - (A - 31 (<strong>2.</strong>15)<br />

A transistor was first used as a sensor in the thermal conductivity detector in 1972<br />

[31], its use being based on the direct conversion of changes in the sensor temperature<br />

into an electric signal. As transistors cannot be heated directly, they are maintained<br />

at a temperature T, by an external source. <strong>The</strong> steady-state thermal equilibrium can<br />

be expressed in terms of the transistor collector current, I,:<br />

I, E = 0 . R (T, - T,) (<strong>2.</strong>16)


<strong>The</strong> sensor temperature, T,, changes during the elution and the change is manifested<br />

in a change in the collector current, AI,, which is measured directly. A bridge circuit is<br />

not used and this method leads to a considerable increase in sensitivity.<br />

<strong>2.</strong>3.<strong>2.</strong>1 Seiisor heating voltage<br />

In contrast to the heated filament detector, the dependence of the SrcD obtained<br />

with a thermistor on the voltage exhibits a maximum. <strong>The</strong> optimum value of the<br />

heating voltage is given by the relationship<br />

E,,, - J (RO . 6. Rc . T,) (<strong>2.</strong>17)<br />

Under constant thermistor parameters, i.e., standard-state resistance, Ro, and ma-<br />

terial constant, 6, and with a given carrier gas characterized by a thermal conductivity<br />

Kc, the optimum temperature of the supply voltage depends solely on the temperature<br />

of the detector walls (see Fig. <strong>2.</strong>5).<br />

FIG. <strong>2.</strong>5. <strong>The</strong> dependence of the relative<br />

magnitude of SrCD on the heating voltage<br />

and the detection block temperature;<br />

a, b - thermistor, c - heated filament.<br />

49<br />

Fig. <strong>2.</strong>6. <strong>The</strong> dependence of S<strong>TCD</strong> on the<br />

carrier gas quality; 1 - nitrogen,<br />

2 - hydrogen.<br />

A change in the carrier gas results in a change in the optimum heating voltage.<br />

As follows from the introductory section, carrier gases with lower molecular weights<br />

absorb more heat and therefore a larger heat supply is necessary in order to maintain<br />

the same sensor temperature and a similar sensitivity. This dependence is depicted<br />

schematically in Fig. <strong>2.</strong>6.<br />

<strong>2.</strong>3.<strong>2.</strong>2 Sensor pararneters<br />

<strong>The</strong> signal of the thermal conductivity detector with a heated filament depends on the<br />

properties of the filament, especially on its specific resistance, e, and its thermal


50<br />

coefficient, a. <strong>The</strong> signal is related to these values by the relationship<br />

S<strong>TCD</strong> - alJe<br />

<strong>The</strong> values of a, e and S<strong>TCD</strong> for some materials are summarized in Table <strong>2.</strong>4.<br />

TABLE <strong>2.</strong>4<br />

THE SPECIFIC RESISTANCE, THERMAL COEFFICIENT<br />

AND THE RELATIVE RESPONSE OF SOME MATERIALS<br />

USED AS <strong>TCD</strong> SENSORS<br />

Material a. 103[K-'] p [Q. mm2/m] s<strong>TCD</strong><br />

Platinum 4.0 0.106 13<br />

Pt-Ir 90-10 1.2 0.24 <strong>2.</strong>5<br />

80- 20 0.8 0.31 1.5<br />

Tungsten 4.54 0.058 19<br />

Nickel 4.91 0.072 18<br />

(<strong>2.</strong>18)<br />

One of the most commonly used materials is platinum, which, however, has poor<br />

mechanical properies; the filament diameter is therefore generally rather large (about<br />

0.02 mm). Alloys of platinum with iridium or rhodium have better mechanical proper-<br />

ties but yield smaller signals then platinum sensors. After platinum, tungsten is the<br />

most commonly used filament material. Its relative response is comparable with that<br />

of platinum and it also has very satisfactory mechanical properties, so that very thin<br />

filaments (down to 0.006 mm) can be used. However, it is oxidizeh by atmospheric<br />

oxygen at temperatures above 500 "C. Nickel filaments are occasionally used in<br />

corrosive media, but their use is limited by their poor mechanical properties [8, 9,<br />

13, 15, 36, 441.<br />

A number of workers have tried to prolong the life-time of sensors, decrease the<br />

noise level and prevent drift of the background current. In addition to passivation of<br />

the W-Re filament at 330 "C by formation of oxides [8], the surface of the filament<br />

was gilded [17] and treated with HF [15] or CH,Cl, [36] vapour. <strong>The</strong>se modifi-<br />

cations led to an increase in the detector stability. <strong>The</strong> measuring filament has also<br />

been covered with a palladium catalyst [13], increasing the sensitivity for both<br />

a- and p-olefins.<br />

<strong>The</strong>rmistors are characterized by the values of Ro and the material constant. <strong>The</strong><br />

thermistor resistance varies within a wide range, from 1 to lo6 0. In general, the<br />

detector can be used at higher temperatures if a high-resistance thermistor is em-<br />

ployed, but a recorder with a high input impedance must be used. As the sensitivity<br />

of the thermistor to temperature changes is highest at low temperatures, thermistors<br />

with low resistances (of the order of lo3 to lo4 62) can be employed.<br />

<strong>The</strong> thermistor material constant corresponds to the energy required to increase


the temperature by AT,. Hence it is evident that, with increasing material constant,<br />

the detector time constant will increase, thus rendering the results less reliable.<br />

<strong>2.</strong>3.<strong>2.</strong>3 Cell geometric constant<br />

<strong>The</strong> amount of heat removed from the surface of a heated filament is proportional to<br />

its surface area (see equation (<strong>2.</strong>6)). For a cylindrical body, this geometric constant<br />

is given by the relationship<br />

51<br />

(<strong>2.</strong>19)<br />

where 1 is the length of the heated filament, rc is the internal radius of the cell and rf<br />

is the external radius of the filament. It follows from equations (<strong>2.</strong>6) and (<strong>2.</strong>19) that<br />

S<strong>TCD</strong> increases with increasing length and radius of the heated filament and is inversely<br />

proportional to the cell radius. <strong>The</strong>se dependences must be evaluated correctly, as it<br />

is impossible simultaneously to lengthen the filament and make the cell volume smaller.<br />

If the filament is lengthened, the cell must be larger and the detector volume increases;<br />

this leads to an increase in the detector time constant. Existing commercial detectors<br />

represent a compromise among the above requirements. <strong>The</strong> effect of the geometric<br />

constant on the magnitude of the <strong>TCD</strong> signal is represented schematically in Fig. <strong>2.</strong>7.<br />

0 M 15 -a<br />

I<br />

m<br />

FIG. <strong>2.</strong>7. <strong>The</strong> dependence of the FIG. <strong>2.</strong>8. <strong>The</strong> dependence of S<strong>TCD</strong> on the<br />

<strong>TCD</strong> signal on the geometric constant<br />

at various temperatures of the heated<br />

temperature of the filament and of the cell<br />

walls; the difference (Tf - T,) is plotted<br />

filament. on the x-axis.<br />

When a thermistor is employed as the sensor, it is assumed to be spherical and the<br />

geometric constant is expressed by the relationship<br />

4xrrrc<br />

a = - - 4nrt<br />

rc - rf<br />

(<strong>2.</strong>20)<br />

<strong>The</strong>refore, the signal of a detector employing a thermistor is directly proportional to<br />

its radius.


52<br />

<strong>2.</strong>3.<strong>2.</strong>4<br />

Temperatures of the sensor and the cell walls<br />

From the principle of the thermal conductivity detector, it follows that T, must<br />

generally be larger than T, (when a heated filament is used), so that (T, - T,) 2<br />

I - 200 "C. <strong>The</strong> detector signal is directly proportional to the difference between the<br />

temperatures of the heated filament and the cell walls, from which follow important<br />

conclusions concerning the adjustment of the experimental conditions.<br />

At a selected detection block temperature, SrCD is proportional to the temperature<br />

of the heated filament, i.e., to the heating intensity (Fig. <strong>2.</strong>8); on the other hand, at<br />

a given temperature of the heated filament, i.e., with constant heating, S<strong>TCD</strong> is<br />

inversely proportional to the detection block temperature. In practice, it is most<br />

advantageous to maintain the temperature of the heated filament as high as possible<br />

(taking care not to burn the filament) and the detection block temperature as low as<br />

possible (avoiding condensation of eluted substances in the cell).<br />

When working with columns with programmed temperatures, the possibility of<br />

a decrease in the <strong>TCD</strong> signal must be borne in mind if the detection block is connected<br />

to the column thermostat. During an increase in the temperature of the column<br />

thermostat, the temperature difference (T, - T,) decreases and consequently S<strong>TCD</strong><br />

also decreases.<br />

<strong>The</strong> above rules also hold for thermistor sensors. It has been found experimentally<br />

that the highest measuring sensitivity is attained for a small difference between the<br />

sensor and cell temperatures, (T, - T,) = 35 - 50 "C, while the sensor temperature<br />

should not exceed 100 "C. S<strong>TCD</strong> is strongly dependent on the detection block temperature:<br />

STcD 81.5R1l2T-2 f c (<strong>2.</strong>21)<br />

<strong>The</strong>refore, it is preferable to maintain the detection block temperature as low as<br />

possible.<br />

<strong>2.</strong>3.<strong>2.</strong>5<br />

Time constant of the <strong>TCD</strong><br />

<strong>The</strong> magnitude of the time constant depends on the effective volume of the detector.<br />

<strong>The</strong> requirement that the time constant of the measuring device should be as low as<br />

possible, leading to the smallest possible distortion of the elution curves, is partially<br />

in opposition to the requirements regarding the magnitude of the detector signal<br />

concerning, for example, the length of the heated filament or a large thermistor radius.<br />

<strong>The</strong> cell time constant is expressed by the relationships<br />

and<br />

vdet = ' * 'dst<br />

7 = 0.632td,,<br />

<strong>The</strong>se relationships are valid, however, only for cells in which transport occurs


exclusively through convection. A number of thermal conductivity designs have been<br />

proposed in which both diffusion processes and mass convection towards the sensor<br />

surface participate. According to this criterion, cells are classified as flow-through,<br />

semi-diffusion and diffusion. <strong>The</strong> shapes of these cell types are depicted in Fig. <strong>2.</strong>9.<br />

FIG. <strong>2.</strong>9. Various shapes of thermal conductivity cells; a - flow-through,<br />

b - diffusion, c - semi-diffusion.<br />

<strong>The</strong> expression for the time constant of flow-through cells reflects the significant<br />

dependence of their signal on the gas flow-rate. <strong>The</strong>refore, manostats are placed<br />

before the cells in order to stabilize the flow-rate and the pressure [12]. <strong>The</strong> smallest<br />

distortion of the shape of the elution curve is achieved with a low time constant;<br />

designers of thermal conductivity cells thus attempt to make the flow-through cell<br />

volume as small as possible. Cells with volumes of 20 pI [21], <strong>2.</strong>6 ,d [32] and even<br />

1 pL1[23] have been described.<br />

TABLE <strong>2.</strong>5<br />

TIME CONSTANTS OF VARIOUS CELL TYPES<br />

IN THERMAL CONDUCTIVITY DETECTORS<br />

Cell 7 [sec] Notes<br />

Flow-through 0. I- 1 most frequently used, most<br />

sensitive to all changes<br />

Diffusion 10-20 unsuitable for modern<br />

measuring requirements<br />

Semi-diffusion o1 /r2 > 1 up to 10 properties of the flow-through cell<br />

CI/U2 J. 1 up to 20 properties of the diffusion cell<br />

53


54<br />

It is obvious that the time constant will increase with increasing participation of<br />

diffusion in the transport process. <strong>The</strong> time constant of a semi-diffusion cell can be<br />

expressed by the relationship<br />

1<br />

z = 0.632t,,, -<br />

2-- V<br />

111<br />

where trl is the gas flow-rate through the measuring branch (see Fig. <strong>2.</strong>9). <strong>The</strong> time<br />

constants of the cell types discussed are listed in Table <strong>2.</strong>5. In addition to the time<br />

constant of the measuring cell, the sensor time constant, determined by its mass and<br />

heat capacity, must also be considered. Thus the sensor requires a certain time to<br />

record a change. <strong>The</strong> time constant of a heated filament is given by the relationship<br />

As the heat capacity of the filament is proportional to its volume, i.e., mC, - $1, the<br />

requirement of high <strong>TCD</strong> sensitivity (see equations (<strong>2.</strong>9) and (<strong>2.</strong>19)) leads to an<br />

increase in the sensor time constant. <strong>The</strong> heat capacity of the thermistor approxima-<br />

tely equals the material constant, 6, and varies around 1 sec for most sensors of this<br />

type. In a provisional arrangement, the transistor sensor had a large time constant<br />

of 10 sec [31], which the authors felt could be decreased to 0.6 sec.<br />

In some designs, the heated filament is sealed in glass in order to decrease the<br />

catalytic action of the heated filament on the thermal decomposition of substances<br />

and to prevent corrosion of the sensor. Similarly, materials other than glass have also<br />

been employed, e.g., fluorinated plastic [5]. <strong>The</strong>se modifications lead to an increase<br />

in the lifetime of the sensor and make its use at higher temperatures possible, but the<br />

TABLE <strong>2.</strong>6<br />

THE TIME CONSTANT OF THE THERMAL CONDUCTIVITY DETECTOR<br />

Cell<br />

Sensor<br />

heated filament<br />

filament in thermistor transistor<br />

Length of cell<br />

- sensor [cm]<br />

2 10 2 0.2 0.2<br />

Diameter of cell<br />

- sensor [cm]<br />

0.5 0.002 0.1 0.2 0.2<br />

Gas flow-rate [ml/min] 30<br />

Time constant [sec] 0.45 0.01 4 1 9.6


time constant of the sensor and consequently that of the whole detector are increased<br />

considerably due to an increase in the heat capacity of the measuring element. Cell<br />

time constants and those of individual sensor types are given in Table <strong>2.</strong>6, from<br />

which it follows that a heated filament has the lowest time constant. It should be<br />

used in combination with a flow-through cell whenever theoretical or quantitative<br />

empirical conclusions are to be made on the basis of the measured results.<br />

<strong>2.</strong>3.<strong>2.</strong>6 Measuring circuits<br />

If a heated filament or thermistor is used as a sensor in the thermal conductivity<br />

detector, it is connected in a Wheatstone bridge for compensation measurements.<br />

When a voltage E is brought to a bridge consisting of the sensor resistance, R,,<br />

and a reference sensor resistance, R,, then, for the current passing through the circuit<br />

(Fig. <strong>2.</strong>10)<br />

_-<br />

.I<br />

U<br />

E = I(R, + R,)<br />

A signal corresponding to the voltage change due to a change in the sensor resistance<br />

can be measured at the bridge output.<br />

f f<br />

FIG. <strong>2.</strong>10. Scheme of the<br />

FIG. <strong>2.</strong>1 1. Scheme of the <strong>TCD</strong> circuit with a constant<br />

<strong>TCD</strong> constant-current circuit. sensor temperature.<br />

<strong>The</strong> above principle is used in both constant-current and constant-voltage circuits,<br />

with either two or four sensors. A single thermistor in a voltage-powered bridge has<br />

also been employed [7]; however, the only advantage of this circuit was its simplicity,<br />

the JCD parameters not being improved. In addition to the measurement of d.c.<br />

voltage and current, square-wave JCD operation has also been proposed. Constant-<br />

current bridges yield a broader linear dynamic range than constant-voltage bridges.<br />

Recently, a thermal conductivity detector with a constant sensor temperature was<br />

introduced [49]. In this circuit, a single variable resistor is connected in the bridge<br />

(Fig. <strong>2.</strong>11). <strong>The</strong> uncompensated output voltage is amplified and fed back to the bridge<br />

55


56<br />

through a transistor controlling the current passing through the bridge. In this<br />

way, the current is instantaneously adjusted so that the sensor resistance, R,, and<br />

consequently its temperature, T,, do not change.<br />

It has been found experimentally that a device with a constant-temperature<br />

sensor has a number of advantages over constant-voltage or constant-current circuits.<br />

<strong>The</strong> lowest detectable amount is decreased ten-fold, the linear dynamic range is<br />

broader by one order of magnitude and the detector time constant is decreased.<br />

Concentrations of 10% by volume were measured in this way without a change in the<br />

detector linearity.<br />

<strong>The</strong> pronounced improvement in the JCD parameters when a constant temperature<br />

is used can be explained by the fact that, owing to the constant sensor temperature<br />

during the elution, the entire elution curve is measured under constant conditions<br />

with constant sensitivity. With constant-voltage or constant current circuits, the<br />

sensor temperature gradient follows the concentration gradient of the eluted substance.<br />

With increasing amounts of eluted substances, the measuring sensitivity decreases<br />

owing to a decrease in the sensor temperature.<br />

<strong>2.</strong>4 APPLICATIONS OF THE <strong>TCD</strong><br />

<strong>The</strong> thermal conductivity detector is one of the most commonly used detectors in gas<br />

and liquid-solid chromatography [41]. In addition to a number of reviews [17, 19,<br />

TABLE <strong>2.</strong>1<br />

EXAMPLES OF THE APPLICATION OF THE THERMAL CONDUCTlVITY<br />

DETECTOR<br />

Substance determined Material analyzed <strong>The</strong> lowest detect- Ref,<br />

able amount<br />

Permanent gases in air<br />

Permanent gases in chlorine<br />

Permanent gases<br />

in high purity ethylene<br />

N2, 02, c02<br />

in exhaled air<br />

NO, in air<br />

0 in organic compounds<br />

N in organic compounds<br />

Metal halides<br />

PCI,<br />

Chlorinated hydrocarbons<br />

Alkanes, alcohols, aliphatic acids<br />

Olefins, branched olefins<br />

‘BH18; C10H22;<br />

0.002 1.11 10, 23,<br />

35,43<br />

I1<br />

17a<br />

30<br />

3a<br />

27<br />

1 1.1g 39<br />

1.9 x mole 5<br />

8.7 X mole 5<br />

15<br />

37<br />

13<br />

1.4; <strong>2.</strong>7; 3.5ppm 32


24, 33, 34, 42, 481, the excellent treatment of the <strong>TCD</strong> in the book by Jentzsch and<br />

Otte [18] should be mentioned. Some examples of <strong>TCD</strong> applications are given in<br />

Table <strong>2.</strong>7. When the <strong>TCD</strong> is compared with other detectors, for example the discharge<br />

detector [l], E CD [5] or FP D [14], better parameters are usually found for the <strong>TCD</strong>.<br />

Comparison of the <strong>TCD</strong> with the FID [4, 35, 371 depends on the structures of the<br />

eluted substances. <strong>The</strong> <strong>TCD</strong> is, of course, more suitable for inorganic gases such as<br />

CS,, COS, H,S and SO, [35]. During measurement of the signal ratio, S"/SrCD,<br />

n<br />

FIG. <strong>2.</strong>1<strong>2.</strong> Analysis of air using a <strong>TCD</strong> with a transmodulator [23].<br />

values greater than unity were obtained for alkanes, and values smaller than unity for<br />

oxygen-containing compounds [37]. It can be presumed that the thermal conductivity<br />

detector will find further use in analyses of inorganic gases, of silylated samples, etc.<br />

[26]. A thermal conductivity detector with a palladium transmodulator [23] gave<br />

excellent results in analyses for rare gases in air (Fig. <strong>2.</strong>12).<br />

<strong>2.</strong>5 LITERATURE<br />

I. Arnikar H. J., Rao T. S., Karmarkar K. 13.: J. Chrornatogr. 38, 126 (1968)<br />

<strong>2.</strong> Barry E. F., Rosie D. M.: J. Chrorwtogr. 59. 269 (1971)<br />

3. Barry E. F., Jr.: Chenz. Abslr. 76, 50 486c (1972)<br />

3a. Beskova G. S., Filipov V. S.: Zaaod. Lab. 38, 154 (1972)<br />

4. Bogoslovskii Yu. N., Razin V. L.: Zlz. Fiz. Khim. 45, 2490 (1971)<br />

5. Brazhnikov V. V., Sakodynskii K. I.: Clzern. Absrr. 74, 94 013j (1971)<br />

6. Castello G., DAmato G.: J. Chromatogr. 32, 625 (1968)<br />

7. Chowdhury B., Karasek F. W.: J. Chroniatogr. Sci. 8, 199 (1970)<br />

8. Cieplinski E. W., Spencer S. F., Illingsworth W. L.: US Pat. 3,537,914 (Nov. 3, 1970)<br />

57


58<br />

9. Delew R. B.: J. Chromatogr. Sci. 10, 600 (1972)<br />

10. Ediz S. H., van Swaay M., McBride H. D.: Chem. Instruni. 3, 299 (1972)<br />

11. Gerdes W. F.: US Pat. 3,474,661 (Oct. 28, 1969)<br />

1<strong>2.</strong> Goryunov Yu. A,, Zalkin V. S., Okhotnikov B. P., Rotin V. A., Rozanova L. I., Maksimov<br />

B. G.: USSR Pat. 371 511 (Feb. 22, 1973)<br />

13. Guillot J., Bottazzi H., Gyuot A., Trambouze Y.: J. Gas Chromatogr. 6, 605 (1965)<br />

14. Gutsche B., Herrmann R.: <strong>2.</strong> Anal. Chem. 249, 168 (1970)<br />

15. Hachenberg H., Gutberlet J.: Brensf. Chem. 49, 242 (1968)<br />

16. Hara N., Katsuda M., Kato H., Hasegawa K., Ikebe K.: Chem. Abstr. 68, 65 5D4r (1968)<br />

17. Hartmann C. H.: Anal. Chenz. 43, 113A (1971)<br />

17a. Jadrijevic V., Deur-Siftar D.: Chromafogruphia 7, 19 (1974)<br />

18. Jentzsch D., Otto E.: Detektoren in der Gas Chromatographie, Akademische Verlaggeselschaft,<br />

Frankfurt a. M. 1970<br />

19. Johns T., Stapp A. C.: J. Chromatogr. Sci. 11, 234 (1973)<br />

20. Karp S., Lowell S.: Anal. Chern. 43, 1910 (1971)<br />

21. Kiefer M. E.: Ger. Offen. <strong>2.</strong>222 617 (Nov. 30, 1972)<br />

2<strong>2.</strong> Lindsay A. L., Bromley L. A,: Ind. Eng. Chem. 42, 1508 (1950)<br />

23. Lovelock J. E., Simmonds P. C., Shoemake G. R.: Anal. Chem. 43, 1958 (1971)<br />

24. McNair H. M., Chandler G. D.: J. Chromatogr. Sci. 11, 454 (1972)<br />

25. Monfort J. P.: Chim. Anal. (Paris) 53, 646 (1971)<br />

26. Morrow R. W., Dean J. A., Shults W. D., Guerin M. R.: J. Chromatogr. Sci. 7, 572 (1969)<br />

27. Nikolaeva N. A., Dolgopolskaya P. I., Rezler R. Yu.: Chem. Abstr. 70, 111 448s (1969)<br />

28. Novik J., WiEar S., Janak J.: Coll. Czech. Chem. Commun. 33, 3642 (1968)<br />

29. Novak J., Janiik J.: Coll. Czech. Chem. Commun. 35, 212 (1970)<br />

30. Noviik J., JaniEek M.: Chem. Listy 65, 739 (1971)<br />

31. Otte E., Gut J.: Chromatographia 5, 246 (1972)<br />

3<strong>2.</strong> Pecsar R. E., De Lew R. B., Iwao K. R.: Ana. Chem. 45, 2191 (1973)<br />

33. Richmond A. D.: J. Chrornatogr. Sci. 9, 92 (1971)<br />

34. Rosie D. M., Barry E. F.: J. Chromatogr. Sci. 11, 237 (1973)<br />

35. Schaeffer B. A.: Anal. Chenz. 42, 448 (1970)<br />

36. Seibel A. C., Johns T.: US Pat. 3,533,858 (Oct. 13, 1970)<br />

37. Sokolov D. N., Golubeva L. K.: Zauod Lab. 35, 143 (1969)<br />

38. Tamura H., Hozumi K.: Chem. Abstr. 72, 128 311f (1970)<br />

39. Thuerauf W.: <strong>2.</strong> Anal. Chem. 250, 11 1 (1970)<br />

40. Vermont J., Guillemin C. L.: Anal. Chem. 45, 775 (1973)<br />

41. Versino C., Fogliano L., Giaretti F.: Riu. Combust. 21, 389 (1967)<br />

4<strong>2.</strong> Villalobos R.: Chem. Eng. Progr. 64, 55 (1968)<br />

43. Volkov E. F., Rabinovich S. I., Breshchenko V. Ya.: Ref. Zh. Khim. 1969, 5 G 14<br />

44. Wade R. L., Cram S. P.: J. Chromatogr. Sci. 10, 622 (1972)<br />

45. Walsa J. T., McCarthy K. J., Merritt C., Jr.: J. Gas Chromatogr. 6, 416 (1968)<br />

46. Wassiljewa A.: Physik. <strong>2.</strong> 5, 737 (1904)<br />

47. Watanabe S., Nakasato S., Kuwayama H., Sasamoto Y., Shihaishi S., Seino H., Nagai T.,<br />

Negishi M., Hayano S.: Yukagaku 22, 102 (1973)<br />

48. Winefordner J. D., Glenn T. H.: Aduan. Chromatogr. 5, 263 (1968)<br />

49. Wittebrood R. T.: Chromatographia 5, 454 (1972)<br />

50. Zalkin V. S.: Zauod. Lab. 36, 129 (1970)

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