chemical physics of discharges - Argonne National Laboratory
chemical physics of discharges - Argonne National Laboratory chemical physics of discharges - Argonne National Laboratory
220 THE EFFECT OF CORONA ON THE REACTION OF CARBON MONOXIDE AND STEAM T.C. Ruppel, P.F. Mossbauer, and D. Bienstock U.S. Department of the Interior, Bureau of Mines, Pittsburgh Coal Research Center, Pittsburgh, Pa. SUMMARY I The water-gas shift reaction was chosen for study in a corona discharge with the aim of establishing the important variables associated with the production of hydrogen. The reaction was carried out in a quartz Siemen's type ozonizer having an electrode length of 12 inches and an electrode separation of 8 nun. The electrodes consisted of fired-silver paint--one electrode coating the inside of the inner (high voltage) tube, and the other coating the outside of the outer (ground) tube. The reaction was studied by means of a four-factor, two-level, factorially designed set of experiments. This consisted of input power levels of 60 and 90 watts,. pressures of .Si and 1 atmosphere, hourly space velocities of 200 and 800, and reactor temperatures of 127 and 527OC (400 and 800'K). Although voltage was not a factor, the voltage ranged from 3100 to 11,000 rms volts. The prediction equation resulting from the statistical analysis of the data indicates that more hydrogen is produced at higher pressures, temperatures, and power inputs, and lower space velocities. Practically no hydrogen is produced in the absence of a discharge, regardless of the values of space velocity, temperature, pressure, or power dissipated. The highest yield of hydrogen within the factorial region studied was 4.5 per- cent. An extra-factorial region, which was indicated by the prediction equation to be fruitful, was explored and 11.5 percent hydrogen was obtained. It was found that the water-gas shift reaction in a corona discharge is kinetically, rather than thermodynamically controlled. INTRODUCTION Novel techniques are being investigated at the Bureau of Mines to introduce energy into coal and coal products in an effort to find new uses for coal. One technique under study involves chemical reactions in a corona discharge. Initially the gas-phase reaction of carbon monoxide and steam to produce carbon dioxide and hydrogen will be investigated. The immediate aim of this studv is to establish the imoortant variables associated with the production of hydrogen in the water-gas shift reaction in the presence of a corona discharge. A more general goal is to determine the dependence of product yield on the important variables in a corona discharge for several gas-phase reactions' As knowledge is gained on the effect of corona discharge in chemical reactions, mre complex reactions involving coal and its products will be studied. 4 < The water-gas shift reaction, which is usually carried out industrially over an Fefl3-Cr203 catalyst at 300-500°C and 100-300 psig, has been discussed at great length in the literature. Summary articles are a~ailable.l-~ It is almost certain- / ' ,' ly a surface reaction5 as opposed to the apparent homogeneous nature of the reaction ; in the corona discharge. Experiments with the quartz Siemen's type ozonizer to be described have shown that no reaction occurs between water and carbon monoxide at ,p i
7 h \ F 221 600°C and 1 atmosphere pressure in the absence of a corona. This suggests that the reaction is homogeneous when it does occur with a corona. That is, the reactor walls probably do not enter into the reaction by acting as a catalyst or as a third body. The physics6-8 and chemistry9-" of corona discharge have been surveyed by several authors. A bibliography of chemical reactio s in electrical discharges over a thirty-year period, 1920-1950, has been compiled. 19 PROCEDURE The corona discharge unit is shown in figure 1. The operational scheme can be seen in the flow diagram, figure 2. Carbon monoxide from a compressed gas cylinder (1) is passed through an activated carbon adsorption trap (5). The metered flow (7) passes through a flow control valve (9); a second stream of gas may be blended here if desired. The carbon monoxide at the pressure of the system passes through a steam generator (11). The thermocouple immediately above the reflux condenser (17) controls the steam flow rate via a time-proportionating temperature controller (not shown). The carbon monoxide and water flow rates may be individually varied between 0.2 and 3 ft.3fhr. by adjusting the flow controller (9) and temperature controller settings. The carbon monoxide-steam mixture then enters the Siemen's-type reactor through preheaters (18) and (21). The reactor is enclosed in a tube furnace (23). The product gases pass through a series of three cold traps (25, one shown) at -8OOC. Bypass cold traps (26) are available if required. The non-condensable gases pass through a sample train (28,29) and then through a flow meter (30) which is at system pressure. On leaving the flow meter the non-condensable gases pass through the system-pressure regulator (32), vacuum pump (34), and finally a wet test meter (35). The system is designed to operate from 0.5 to 2.0 atmospheres. The Siemen's type reactor, shown in figures 3 and 4, consists of two concentric quartz tubes, 45 and 33 mm. OD, having a 4 mm. annular space. The electrode length is 12 inches and there is an 8 mm. electrode-to-electrode separation. The electrodes consist of fired-silver paint--one electrode coating the inside of the inner (high voltage) quartz tube, and the other coating the outside of the outer (ground) tube. Tungsten (or optionally copper) wires are attached to the outside and inside of the reactor with two or three coatings of fired-silver paint. The capacitance of the reactor was measured as 86-89 pfad using an impedance bridge. The average wall temperature was used as a measure of the temperature of the system. Three thermocouples were equally spaced vertically along the inside wall of the reactor (fig. 2) and three along the outside wall. The inside wall thermocouples were at the corona potential and thus were isolated from ground. A millivoltmeter was connected in series to each of the inside wall couples, and thus was similarly "floated". To simplify the electrically hot thermocouple circuits, no compensating ice junction was included; the room temperature correction was added to each millivoltmeter reading. The corona potential had a positive effect on the millivoltmeter readings in the hot circuit. Therefore the millivoltmeters were read before the corona potential was impressed on the system. taken as the average of all six thermocouple measurements. The system temperature was The study was made according to a factorially designed set of experiments to determine the effect of pressure, space velocity, temperature, and input electrical power on the yield of hydrogen. This was a four factor, two level set of experiments as shown in Table 1. I
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7 h<br />
\ F<br />
221<br />
600°C and 1 atmosphere pressure in the absence <strong>of</strong> a corona. This suggests that the<br />
reaction is homogeneous when it does occur with a corona. That is, the reactor walls<br />
probably do not enter into the reaction by acting as a catalyst or as a third body.<br />
The <strong>physics</strong>6-8 and chemistry9-" <strong>of</strong> corona discharge have been surveyed by<br />
several authors. A bibliography <strong>of</strong> <strong>chemical</strong> reactio s in electrical <strong>discharges</strong> over<br />
a thirty-year period, 1920-1950, has been compiled. 19<br />
PROCEDURE<br />
The corona discharge unit is shown in figure 1. The operational scheme can be<br />
seen in the flow diagram, figure 2. Carbon monoxide from a compressed gas cylinder<br />
(1) is passed through an activated carbon adsorption trap (5). The metered flow (7)<br />
passes through a flow control valve (9); a second stream <strong>of</strong> gas may be blended here<br />
if desired. The carbon monoxide at the pressure <strong>of</strong> the system passes through a<br />
steam generator (11). The thermocouple immediately above the reflux condenser (17)<br />
controls the steam flow rate via a time-proportionating temperature controller (not<br />
shown). The carbon monoxide and water flow rates may be individually varied between<br />
0.2 and 3 ft.3fhr. by adjusting the flow controller (9) and temperature controller<br />
settings. The carbon monoxide-steam mixture then enters the Siemen's-type reactor<br />
through preheaters (18) and (21). The reactor is enclosed in a tube furnace (23).<br />
The product gases pass through a series <strong>of</strong> three cold traps (25, one shown) at<br />
-8OOC. Bypass cold traps (26) are available if required. The non-condensable gases<br />
pass through a sample train (28,29) and then through a flow meter (30) which is at<br />
system pressure. On leaving the flow meter the non-condensable gases pass through<br />
the system-pressure regulator (32), vacuum pump (34), and finally a wet test meter<br />
(35). The system is designed to operate from 0.5 to 2.0 atmospheres.<br />
The Siemen's type reactor, shown in figures 3 and 4, consists <strong>of</strong> two concentric<br />
quartz tubes, 45 and 33 mm. OD, having a 4 mm. annular space. The electrode length<br />
is 12 inches and there is an 8 mm. electrode-to-electrode separation. The electrodes<br />
consist <strong>of</strong> fired-silver paint--one electrode coating the inside <strong>of</strong> the inner (high<br />
voltage) quartz tube, and the other coating the outside <strong>of</strong> the outer (ground) tube.<br />
Tungsten (or optionally copper) wires are attached to the outside and inside <strong>of</strong> the<br />
reactor with two or three coatings <strong>of</strong> fired-silver paint. The capacitance <strong>of</strong> the<br />
reactor was measured as 86-89 pfad using an impedance bridge.<br />
The average wall temperature was used as a measure <strong>of</strong> the temperature <strong>of</strong> the<br />
system. Three thermocouples were equally spaced vertically along the inside wall <strong>of</strong><br />
the reactor (fig. 2) and three along the outside wall. The inside wall thermocouples<br />
were at the corona potential and thus were isolated from ground. A millivoltmeter<br />
was connected in series to each <strong>of</strong> the inside wall couples, and thus was<br />
similarly "floated". To simplify the electrically hot thermocouple circuits, no<br />
compensating ice junction was included; the room temperature correction was added to<br />
each millivoltmeter reading. The corona potential had a positive effect on the<br />
millivoltmeter readings in the hot circuit. Therefore the millivoltmeters were read<br />
before the corona potential was impressed on the system.<br />
taken as the average <strong>of</strong> all six thermocouple measurements.<br />
The system temperature was<br />
The study was made according to a factorially designed set <strong>of</strong> experiments to<br />
determine the effect <strong>of</strong> pressure, space velocity, temperature, and input electrical<br />
power on the yield <strong>of</strong> hydrogen.<br />
This was a four factor, two level set <strong>of</strong> experiments as shown in Table 1.<br />
I