Boiling Points of Electrolytic Caustic Solutions - Industrial

Ind. Eng. Chem. , 1929, 21 (1), pp 40–42. DOI: 10.1021/ie50229a012. Publication Date: January 1929. Cite this:Ind. Eng. Chem. 21, 1, 40-42. Note: In...
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Vol. 21, No. 1

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Boiling Points of Electrolytic Caustic Solutions' C. C. Monrad and W. L. Badger UKIYERSITY OF MICHIGAN, AKNARBOR,~ I I C H .

N A previoue publication by one of the authors2the discrepancies in the existing information on the boiling points of electrolytic caustic solutions were indicated. Shortly after that paper was written, work was begun on a redetermination of boiling points of these solutions with the hope that data could be obtained of greater accuracy and over a wider range than heretofore. I n the interval Adams and Richards3 published the results of Pink, which confirmed fairly well some of the figures used by Badger in his article. Since caustic evaporators are now in operation with working temperature drops of less than 10" C., it is obvious that an accuracy of * 1' C. is no longer within the limits of commercial requirements. The method of prediction advocated by Adams and Richards involves errors of several degrees for solutions boiling under considerably diminished pressure. The present series of data are so much more complete and of so much greater precision than anything a t present in the literature that they will be presented in considerable detail.

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Apparatus

Previous workers had used glass apparatus, which is open t o the objection that glass is rapidly attacked by strong caustic August 2, 1928. SBadger, Trans. Am. Inst. Chem. Eng., 18, 231 (1926). * I N D .ENQ. CHRM.,20 470 (1928). 1 Received

solutions. Pink not only used glass apparatus but immersed the thermometer directly in the solution to be examined. This causes errors due to superheating and possibly smaller errors due to hydrostatic head, The apparatus used in this investigation is a modification of that described by Baker and Waite4 and is illustrated in Figure 1. A is a boiling vessel made of monel with a suitab!e cover carrying a monel tube as a vapor pipe. Into the bottom of the bomb was inserted a closed monel tube, A , in the interior of which was inserted a chrome1 heating element wound on Usalite tubing. Over this heating element stood the modzed Cottrell pumping tube, C, made entirely of monel. The side outlet to the bomb used for withdrawing samples was also of monel. The vapor pipe was surrounded by an iron condenser, D, and contained the precision platinum resistance thermometer, E. The glass tube which formed the casing of this thermometer was first silvered and then nickel-plated so that the solutions came in contact only with monel or nickel. A short connection led directly from the vapor space to the barometermanometer combination, F , from which the absolute pressure could be read as the difference in the two mercury columns. From the vapor pipe another glass tube led t o the vacuumproducing and -regulating system. This consisted of a 12liter flask, H , for damping out fluctuations in the pressure, (r

Tans. Am.

Inst. Chem. Eng., 13, P t . 11, 233 (1921).

January, 1929

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poffa and Sommer.' These two sets of determinations checked so closely that in the present work sodium chloride was not determined. From the known temperature and caustic concentration of the samples, the concentration of sodium chloride was calculated, and thus the ratio of sodium hydroxide to water was determined. For any one sample this is constant a t all temperatures, irrespective of the sodium chloride content. Table I-Thermometer

c.

0

O

for Determination of Boiling Points of Caustic Solutions

connected to a water trap, I , and this through N t o a laboratory water-jet vacuum pump. The trap I was connected to a manometer, M , on the high side of which was a platinumtipped brass rod, L. As the vacuum rose it made a contact between the mercury and this rod, closed a battery circuit through the relay K , which then closed the 220-volt circuit through solenoid J and opened the needle valve 0, admitting air to the system. By means of a stop which limited the travel of the needle valve to a fraction of a millimeter, it was possible to maintain the vacmm as shown by manometer -11 constant to within 1 or 2 mm., and these fluctuations were so removed by the flask H that the manometer F showed variations of the order of 0.2 mm. The Cottrell pumping tube kept the thermometer covered with a film of the boiling liquid in equilibrium with the vapor and prevented overheating a t this point. The

ance thermometer was calibrated against ice and steam, with the results shown in Table I. 11 The solutions were made up from caustic soda purified by alcohol and were saturated with so- $ dium chloride. An excess of solid sodium chlo- 5 O' ride was maintained in the boiling vessel a t all times, so that the solutions were saturated a t s their boiling points, as will always be the case in a the commercial caustic evaporators. Since the materials used were relatively pure, these solutions differ from commercial cell liquors by con-

c.

DIFFERENCE

c.

0.01 0.03 0.02 0.00

98.98 53.02 78.81 92.89

98.99 52.99 78.83 92.89

Figure I-Apparatus

Calibration

CALCULATED

ACTUAL

It m7as suspected a t first that a t different temperatures and different rates of boiling the amount of water draining back from the condenser D might not be uniform. For every solution used, samples were withdrawn a t three different pressures and their analyses were substantially identical. This proves that the amount of water in the vapor pipe and on the walls of the condenser did not vary enough t o affect the composition of the liquid. Accuracy of Results

It was not found possible to control the conditions during actual determinations closer than *0.05' C. The agreement of the analyses was so close that the errors could not account for any greater fluctuation in the boiling point than this figure. Further, the boiling point of each solution was determined a t a number of pressures, and in no case did these points deviate more than 0.1 ' C. from the best straight line that could be drawn through them. It is believed that the data here reported are accurate t o within *0.lo C. up to 50 parts caustic per 100 parts water, and to *0.2" C. above that concentration.

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