Submitted by A. W. Ingersoll
Checked by Henry Gilman and L. C. Heckert.
1. Procedure
(
A)
Apparatus.—The reduction is carried out in an
18 by 25 cm. battery jar (Note
1) which is surrounded by a
vessel of cold water. The bottom of the battery jar is just covered with
mercury which serves as the cathode of the cell. The anode is a coil of heavy sheet lead separated from the catholyte by suspending it in a
porous cup. The latter is supported in the battery jar so that it just clears the surface of the mercury (Note
2). The cathode is connected with the circuit by means of a copper wire well insulated with rubber except for one-eighth inch at the end which is immersed in the
mercury. Efficient mechanical stirring is provided for the catholyte. The current used for these experiments was drawn from a
storage battery delivering 30 volts, through a
rheostat and
ammeter each capable of carrying 15 amperes. Current may be taken from any source which will supply 80 to 85 ampere-hours at the rate of 5 to 10 amperes. Several reduction cells of the size described may be run at one time by connecting them in series. The diagram given on
p. 486 shows the arrangement of the apparatus.
(
B)
Reduction of Cinnamic Acid.—After the apparatus is assembled,
2 l. of 7–8 per cent sodium sulfate solution (Note
3) is placed in the battery jar and the porous cup is filled to the same level with more of this solution. The stirrer is started, and
200 g. (1.35 moles) of a good grade of cinnamic acid (Note
4) is suspended in the catholyte. A solution of
35 g. (0.88 mole) of sodium hydroxide in 150 cc. of water is then added at such a rate as to avoid forming lumps of
sodium cinnamate (Note
5). The current is turned on and the rheostat adjusted until a steady current of 5 to 10 amperes is flowing (Note
6). From this point only occasional attention is required. The suspended
sodium cinnamate and
cinnamic acid gradually dissolve as the reduction proceeds. Portions adhering to the walls of the cell should be worked down with a stirring rod and finally with a little water from a
wash bottle. The liquor inside the porous cup should be kept alkaline by adding very concentrated
sodium hydroxide solution at about one-half hour intervals (Note
5). About
110 g. (2.7 moles) will be required. The reduction will require 76 to 80 ampere-hours (Note
7); considerable
hydrogen is evolved near the end. The temperature need not be controlled (Note
8).
When reduction is complete (Note
7) the cathode liquor is decanted or siphoned from the mercury, filtered from traces of solid matter, and acidified with an excess of
sulfuric acid (sp. gr. 1.1). The
hydrocinnamic acid separates as an oil and solidifies on thorough cooling. The yield of crude product, which contains water and other impurities, is
180–200 g. It is purified by distillation under reduced pressure. The product boiling at
194–197°/75 mm. (
145–147°/18 mm.) is colorless and melts at
47.5–48°. The yield of distilled acid is
160–180 g. (
80–90 per cent of the theoretical amount) depending upon the quality of the
cinnamic acid used (Note
4).
2. Notes
1. This is a commercial size. Any sturdy glass vessel of similar dimensions may be used.
2. The lead anode should have about the same surface area as the cathode. The porous cup used was 8 by 21 cm., but similar sizes will do. A
three-legged desiccator plate makes a convenient support for the cup.
3. Any dilute solution of
sodium sulfate may be used. If several runs are to be made, the solution recovered from the filtration of the
hydrocinnamic acid should be neutralized with
sodium hydroxide, diluted if necessary, and used again. Traces of
hydrocinnamic acid contained in this solution are thus saved. Chemically pure reagents are not necessary.
4. The quality of the
cinnamic acid used is important. The yield from a commercial c.p. acid melting at
132.5–133° was
86–90 per cent. From a lot melting at
131.5–133° obtained by recrystallizing a crude acid with the use of animal charcoal the yield was
81–83 per cent. With a technical grade of material the yield fell, in some runs, below
60 per cent, the reduction mixture foamed considerably, and much high-boiling residue was left on distillation.
5. The addition of too much
sodium hydroxide at this point produces a thick sludge which does not stir well. It should be noted that during the reduction two molecular equivalents of
sodium hydroxide are produced at the cathode and an equivalent amount of
sulfuric acid at the anode.
6. The current may vary somewhat, especially if the anode liquor becomes too dilute or highly acid. The
sodium hydroxide solution added to the anolyte should be concentrated so that the diffusion which always occurs will not dilute the catholyte excessively. High amperage shortens the time required but promotes heating. Seven amperes is a convenient rate.
7. The theoretical quantity of current is 72 ampere-hours. It is necessary to pass an excess of 4 to 8 ampere-hours to insure complete reduction. The end of the reduction is reached when a sample of the catholyte on acidification with excess
sulfuric acid precipitates an oil and no solid.
8. The reaction is favored by moderately high temperatures. Excessive heating may be avoided by reducing the amperage or by placing cold water in the
cooling bath.
9. It may be noted that this process is essentially a sodium amalgam reduction. By the same procedure
β-furylacrylic acid was reduced to
β-furylpropionic in yields of
60–70 per cent. With suitable modifications it may be applied to the reduction of other substances reducible with
sodium amalgam.
3. Discussion
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