_—__’— .Fd -_—’ __’_’— ___— ______d ’4— _'_—.—— ___‘_—_— _____— —_’—. '—._- _———— __—— _—_‘—— ___—__d ‘_——— —_’—— '_—— ’— —_'——- fl. __—_. ’4 ___'—— .___——— _—__—- _'_4— __—_J— ——’ ,—_" ______—_- #— -___’—— TH . ABSORPTION OF HYDROGEN BY ELECTROLYTIC NICKEL THESIS FOR THE DEGREE OF M. S. Alfred Clark 1932 Adsorption of Hydrogen by Electrolytic Nickel A Thesis Submitted to the Faculty of Michigan state College In Pei-tit]. Fulfillment of the Requirements for the degnee of Master of Science Deportnent of Chemistry by Alfred Clark my, 1932. THREE OF CONTENTS Introduction Encories Apporctus and.natericls Procedure Dot. Calculstions Drusflmg Photogrsyh Discussion Summary 9463)- 18 The Adsorption of mogen by Electrolytic Nickel Introduction The physical and chemical preperties of metals are effected by the crystalline structure. x-ray studies in recent years sho' that the structure of metals deposited electrolytically varies with the amount of hydrogen co-deposited. Whether or not such results can be attributed to the gas which is held by the crystals or to a different structure caused by the presence of a g a film on the metal surface during the formation of the crystals is a preposition open to question. Ii'his investigation is limited to the study of the quantity of hydrOgen held by electrolytic nickel together with observations on the factors which effect the amount of gas adsorbed and the magnitude of the forces of adsorption. It has been the usual practice until quite recently to de- posit nichsl from acid solutions of 5.2 - 6.0 pH. It was believed that a more acid solution would permit the evolution of hydrogen and thus cause the nickel to be more brittle. In this connection Phillips (Trans. Am. Elect. Chem. 8%.. L11. 393, 1931) has shown that nickel deposited from solutions of greater acidity may be rather soft ... at least not more brittle than nickel from solutions ranging from a pH of 5.2 - 6.0. It sears from the work of Phillips that the temperature is a more important factor than acidity in the determination of the hardness of a deposit. 2. Theories Benton and White (J.A.S.S. 52, 2325, 1930) have given evi- dence for assuming two distinct types of adsorption of hydrogen upon nickel: Phylical adsorption prevalent at very low temperatures and decreasing rapidly from -210 to ~18?» deg. 0., until at higher temp- eratures this type of adsorption is entirely superceded by chemical or activated adsorption. The physical or "secondary” type of ad- sorption as it is sometimes called involves only the hydrogen molecules whereas in "primary" or chemical adsorption, the molecules suffer an activation or even complete dissociation. Another type of retention of hydrogen by nickel is the dif- fussion of hydrogen through the nickel. This is not a surface phen- omena, and is comparable to a process of solution. The amount of hydrogen dissolved in nickel is of mmh lower order than that physio- ally adsorbed. Sieverts (Z. Physik. Chem. 60, 129, 1907; 68, 115, 1910; Ber. 42, 538, 1909; 43, 893, 1910; 4.5, 221 and 2576, 1912) has detemined the solubility of several gases in the more cannon metals. His values for the solubility of hydrogen in nickel are as follows; it 764 m. of mercury md at a temperature of 9230 0.. 2.63 cc. of hydrogen were dissolved in 26.97 gms of nickel, whereas at the same temperature and a pressure of 129 m. the solubility had decreased to 0.98 cc. At 822° 0. and 764. me. pressure~ 93.80;“. of hydrogen ; were dissolved and this value decreases to 0.50 cc. at the same temp- erature and a pressure of 52 m. From all of his data on the solution of hydrogen in nickel, Sieverts deduced that the amount dissolved varied as the square root of the pressure. He concluded also that the amount 3. of nickel surface exposed did not effect the amount of hydrogen dis- solved, the amount depending on the weight of the sample. It is evident on this score than that the hydrogen was not being adsorbed at these temperatures. Sieverts gives the following smary in regards to the solubility of various gases in certain metals: HitrOgen: Not dissolved by metals, forms nitrides with aluminum md iron. Carbon dioxide: insoluble in copper. Oxygen: soluble in molten silver. Sulphur dioxide: soluble in molten copper. HydrOgen: soluble in copper, iron, nickel, palladium; insoluble in cadmium zinc, lead, bismuth, tin, antimony, silver and gold. Mayer and Altmayer (Ber. 41, 3063-74, Sept.) take issue with Sieverts on the results which he obtained on nickel, stating that Sieverts did not allow time enough for canplete adsorption. According to Sieverts, the volume of hydrogen taken by by 1 volume ofnickel at 350° C. and 1 atmosphere is 2 volumes. Mayer and Altmayer report 5.5 to 50 volumes of hydrogen per 1 volume of nickel under the same conditions of temperature and pressure. In both cases the nickel was obtained by the reduction from the oxide, Mayer and Altmayer state that the adsorption of hydrogen on nickel is directly proportional to the pressure, thus obeying Henry's Law. Kehlenberg and French (Trans. Am. Elect. Chem. Soc. LIV. 165, 1928) have shown that there is a correlation between the lowering of the potential of a metal electrode when gas is bubbled through the electro- lyte and the adsorptive power of the metal for the gas in question. The 4. greater the adsorptive power of the metal the greater the lowering of potential. Nickel shows a drop superceded only by that of palladiun and platinum. Clausthal (1361:. Phys. Ges.. 1005-22, 1911) carried out some work on the adsorption of hydrogen by various metals at very low temp- eratures. From his experimental results he concluded that the amount of adsorbed gas is conditicned by solution and a surface condensation. Much contradictim exists in data published on the affinity of metals for gases, particularly in the case of adsorption rather than in the case of solubility, where the state of division of the metal, that is, the amount of surface exposed plays so important a role. There is also great confusion as to which of the three types of retention; physical, chemical or solution are taking place under certain conditions. The adsorption of gases on metals appears to be a special case of adsorption of gases on solids, and most of the comnon formulas for such adsorption do not hold even approximately in their case. The amounts of gases adsorbed on metals are all of very low order. Perhaps no gen- eral law of adsorption of gases on solids is possible, for as Langmuir states, the aspects of adsorption may differ greatly from case to case in accordance with the variation in atomic structure and in the kind and distribution of forces in the solid surfaces. The mount of adsorption of gases on the surfaces of metals undergoing a process of electrodeposition, it must be admitted, is a special case of the adsorption of gases upon metals. And even though the some laws, whatever they may be, apply; the conditions such as sur- face area, surrounding media, and surface forces, are so peculiarly char- acteristic that entirely different results may be expected. In the process 5. of electrodeposition of a metal, the integral surface area must be ex- ceedingly large, dependent on the size of the individual nuclei deposited. Apparatus and Materials The apparatus used is show in Drawing 1 and also in the photo- graph. It is entirely of glass and cmsists of a tube (1) wherein the metal is placed, a drying bulb (B) to take up the water vapor adsorbed by the nickel, a manometer (C) for measuring chmges in pressure due to the gas evolved from the metal. ll'he rest of the apparatus is used in purifying the nitrogen which is used as in inert atmsphere, and con- siste of a Tube (D) containing a capper gauze heated by a nichrome wire coil for the purpose of taking the oxygen out of the nitrogen, and a tube (E) to which a drying bulb is attached. The nitrogen can be intro- duced into the main system at will through the two-way stop-cock (P). 1 Bywao Cenco pump was used to produce a vaccumn. (0) is an electric heating unit for driving the gas from the metal , and (H) a theme-couple for measuring the temperature of the unit. Mercury levels were read with a cathetometer to .05 m. The nickel deposit sealed in a small tube was introduced into the vaccunn by breaking the tube with an iron weight lifted by an electromagnet (I). Composition of the nickel electroyteg' The same solution was used throughout the entire experiment and the pH successively lowered by the addition of sulphuric acid. The composition was as folloes: 140 gas. of nickel sulphate per liter. 15 gms. of Boric Acid per liter. 15 gms. of Ammonium Sulphate per liter. 6. Current densities were measured with a millimeter in the electrical circuit. DH measurements were made with the new type Hellige Com- parator, using brom-cresol purple and thymol blue standard color discs and indicator solutions. Nitrogen: 'i'he comercial gas supplied in tanks was used and purified as described. Drying Agent: Phosphorus pentoxide was foumi to be a such more rapid dry- ing agent than magnesium perchlorate, counonly known as anhydrous. The latter was used throughout the work. 7. Procedure The nickel was deposited upon steel plates one square dosimeter in area, ad the deposit peeled from them easily and dried at room temperature. The nickel deposit is placed in a small tube, scaled and placed with a soft iron weight in a larger tube. This larger tube is sealed to the apparatus at (A). The system is then evacuated at J aid sealed off from the pump. Stop-cock (F) is opened to admit nitrogen into the main system enough being ad- mitted to give a pressure of about 100 m., and the stop-cock closed. The tube containing the metal is broken by the iron weight lifted by the electromagnet. The manometer levels are read, and the metal then heated to about 500° c. for thirty minutes. The system is allowed to cool, mercury levels again noted, and enough mercury withdrawn from the manometer through the stop-cock (K) to bring about the same difference in. levels as prior to the heating. One arm of the monster is accurately calibrated in cubic centimeters, and the difference in the mercury levels of this arm before and after heating and adjustment give the volume of the gas expelled from the metal. Tho barometric pressure is taken and the gas values converted to standard conditions. The metal is weighed after the run. The nitrogen is purified in the following manner: With stop-cock (3’) open, the system is evacuated at (1.) and sealed off frm the pulp. Stop-cock (F) is closed and nitrogen admitted until 8. the pressure is approximately atnn spheric as shown by the gauge (M). .We gas is retained here in the presence of the heated copper gauze for fifteen minutes. Stop-cock (F) is then Opened, part of the ni- trogen rushing into (E). (F) is closed and the gas allowed to remain in (E) for fifteen minutes after which time it is ready to be intro- duced into the main system. The copper gauze is reduced at intervals by exposure mile hot, to methyl alcohol vapors. The calibration of the manometer arm was carried out by weighing water drawn out at 2 co. intervals, and then checking against a standardised burrette. Nitrogen was introduced into the apparatus in order to bring the mercury levels to such a position that mercury on be withdrawn without exceeding the limits of the manometer. Oxygen was not used because of the oaralyric action of nickel upon hydrogen and ongen to form water vapor. um..." mono. «0.2. v.3 a .30.: 35.3 flange 2....” «3o. 3.? a.” m mad.» §.Na «3.3 82”.: not" mom a. 3.: v.3. a «35 3a.? 313” 39.2. .3. No.3. mm.n~. noun a 31.3. owns: Hfln.n.n 0023. mm. .33. No.2. aim a Mom; 3.5.9.. 93.: 25.2. 00.0 3.3. No.2. a.” a 03.3 03.2. 30.3 93.3. 8.0 memo. 3.0a aim a 2.9.3 mange 2b.“: «8.2. 8.0 5.80. 3.: fun .n «3.3 3.0.2. «3.3 "3.2. god—3a . a a . meanes- es.” H3. .5 H Ho . amend . shops a « Manson nevus“ masses chemo... \MMJJ H pawns? M 333083 N Lennon. H N 5&2?! H nacho." nope—395” 326” 93865: m6 In as condoned :0»an so even 10. so.n dbflmo Oflodh koNN m @NNsNH flflflafih Ohmonfl “Hmobh mmod Quads Hmanh hoNN m DNHQNH flflwoflfi DwnoOH «@mohb whoa hHmNa @nanh moNN h «Ahead Dhfiomp “finchn nNHamb «Dad Nacho Hooflb moNN b meoHH Ninanb hdkood “@9055 Dead mhflna hmanb 50““ 5 NDQoOH canofih flnoofifl OHhamb omsH "and. QNSVR 00““ m NGOQHH Omflavfi Nflflohfi onwabh .Qhad nfldba onofik moNN 0 Hddom Hanonh Hnfloflfl Hmnomh Hood «can. Omoflfi new“ 0 QdNaHH an00§ anmovfl ommomh fined knows Hdavs boflfl n OOQODH haoamb mOHoOH Duoobb nmaH WNHmo No.05 hoflN n «QHQHH QNNoflh “@QoOH mflfiofih oped “duos omens moNN a Hmhafld nonanb Humahd madcap mfiad ammo. Anods maflN n Ommoflfl DODO¢8 anQOH Ofimabk a ”one; rel . Juneau “ - e wiflttshec e8 . . I Hounds .5 a he a 02:95 . shops a . Epsom no»: . massed muons.» \Nfl .e.o H «swash H unwoaonsm H nuance H «Ic\snnl H cached «39.63 H nacho." nova-83 a...” an as condoned among no «can 11. . on.” some. en.sa e.«« e ooe.en oen.me onm.ma one.nm mn.H coho. 00.05 0.Nu h flonaflfl 000.05 an.0H nnflomm ob.H NHmm. on.is 5.NN h H0H9¢H H09.0b Hflmomd Ham.dm V 00.0 bmmm. «5.05 h.NN H www.md «ufl.wm www.md «an.mm 00.0 000m. Nh.nh new“ H nh¢.0N “00.n0 nb¢.0N unmonm 00.0 hmonofl Hmoeh Daflm H aflmomd HN§.00 0N9.mH HN§.00 «5.6 «naflod nu.¢h b.NN n Hmo.«d nrn.nb HN0.0H .nom.00 0H.~ 05¢».H H00¢s h.NN a 000.0 Ohm.Hb 000.0H nNm.d0 n¢.n 0050. u0.nh b.flN m ammond 0H¢.on MHN.0H maeodo 00.N 0050.H Ghana O.nm m 00b.m 000.nh 0N0.0H non.m0 00.d nflam. amonh ¢.NN n N00.¢H 0H0.hr «00.0N onm.n0 n00.~ anacow 00.05 haw“ n 00H.nn 0H0.mh 000.0H DQO.H0 Oood «N00. 00.05 boflu n 000.0H nn¢.00 m00.Ha Ddoodm H332 . .0 £8 a u may en. « nomads .5 a no ens-none. cusps « . 39sec norms a Masada cacao; \um .06 . “Emacs « nonosog Incense . «5\uans H 323 nope-6g « amoeba usages: a a.» an a. seemeeeq dumeueam as seen 12. Calculations: The calculations are very simple. The following formula express the cubic centimeters of hydrogen per gram of nickel at NgTzP: x = 27Sxp'x X' 760 x T w Where X is the mount of hydrogen adsorbed, p' is the pressure in run. during the run, and w is the weight of the nickel sample. A sample calculation follows: Difference in levels before heating 62.805 om. Difference in levels after heating 62.905 om. Lowering in height of the mercurylevels 5.835 cm. Average Length of Mometer Arm per 00 volume 1.03 can. Volume of gas at 738.6 3 Bar. Press. - 629.05 = 109.55 cm. is z I 5.835 "'1'"?!- 0 Temperature 3 22.7' 0. Weight of sample 3 1.0778 gm. 00 of hydrogen per gram of nickel corrected to NngP: 3'- 273 x 2 x 5.835 x 109.55 : l 503 cc of nickel 750 x 1.03 x 295.7 x 1.0778 ‘ hm ul-i. C . ’— fl —‘ t‘. C. ""Q-U'd-P a. -1 15. Discussion It will be observed on looking at the table of data that the mount of hydrogen adsorbed by the nickel is roughly constant at most current densities and rh's. The results could not as a rule be ex.- actly duplicated, due no doubt to the changing conditions of the electro- 1yte upon continued electrolysis. However, the values lie well within a range of 1/2 cc. The amount of gas adsorbed is logically dependent to some extent on the amount evolved at the cathoue, and indirectly dependent upon the current density and the Ph in so much as these two preperties effect the ratio of the amount of gas adsorbed to the nickel deposited. Beyond a certain point, however, an increase in the amount of hydrogen evolved per unit amount of nickel deposited seems to have no effect upon the amount of hydrogen adsorbed. This may be explained as follows; In the formula, a = 191/ n. expressing the variation in the amount of adsorption, a, with pressure p, k and n being constants characteristic of the adsorbent, when the pressure has reached a certain value, adsorp- tion does not increase, the parabolic curve flattening out into a line practically parallel to the abscissa. It is assumed that at low pressures the number of gas particles are not sufficiently great in number to entirety cover the surface of the adsorbent, thus maximum adsorption does not take place. As the pressure increases, the amber of particles of gas present per unit volume increases, and at some definite pressure the adsorbent may becane entirely covered with the gas particles thus bringing about maximum adsorption. Further increase in pressure will cause no increase in ad- sorption. This is comparable to the case of adsorption during electro- deposition. When the amount of gassing is low enough so that the surface (s 16. of the nickel is not completely covered then.manimum adsorption.will not take place. By lowering the pH or increasing the amount of current, -that is, increasing the amount of gassing, a point will be reached where the gas will completely cover the surface of the metal and further ins creasing of current density or lowering of the pH will not increase the amount of adsorption. In this type of adsorption.then at any constant pH, the current density plays the same role as the pressure in the above formula. Thus it is seen from the data that at l ampere per square decimeter, and a pH of 2.8, no appreciable quantity of hydrogen is ad- sorbed, whereas at 3 amperes per square decimeter 1.5 cc. per gram are adsorbed, which is the average maximum amount adsorbed. Thus somewhere between 1 and 5 amperes is the value of the current density which will just cause maximum adsorption. Now by determining the current efficiencies in this range, the value for the rate of evolution of hydrogen which will Just cause maximum adsorption may be obtained, i.e. the amount of gas which will just completely cover the surface of the nickel. The time of deposition has no appreciable effect on the amount of gas adsorbed, so that the rate of diffusion.may be considered.negligible. The hydrogen is held upon the nickel quite tenaciously; in fact a sample of nickel may be exposed to a vaccuum of 1 or 2 mm. for several hours at ordinary temperatures without releasing its gas. When.heated to approximately 175° C. it commences to lose its gas. Electrodeposited nickel adsorbs some water vapor, but the pre- dominating adsorbed substance is hydrogen, prObably because of the smaller size of the hydrogen molecules, which allow them a greater penetration than the water molecules. 17. Whether the presence of hydrogen has any deleterious effects upon the nature of the nickel deposit was not ascertained. however, it has been shown that whatever may be the ill effects of adsorbed hydrogen they are not increased in the low pH baths where gassing is great er. Of course greater gassing may have a tendency to produce a more honey- combed structure even though the gas may not be adsorbed. A very interesting argument was instigated by an article by Harding and Smith (J.A.C.S., 40, 1508-31, 1918). In this article it was stated that while hydrogen was being deposited upon a metal, the re- sistance first rose to a maximum and then lowered. The rising to a maxi- mum was explained by assuming that during this period an alley was being formed, and the lowering was explained by assuming that a transient type of hydrogen which was conducting was then being formed. Newbery (J.A.C.S., 41, 1887-92, 1919) criticises the formation of a transient hydrogen. He believes that hydrides are formed under the great pressures produced by high current densities, and are decomposed on cessation of the current. He bases his argument on the fact that the single potential of platinum electrode saturated with hydrogen is some- times .72 v. higher than that of the hydrogen electrode and, therefore, a hydride must be assumed. Harding and Smith (J.A.C.S., 41, 1892-4, 1919) return with more proof of their theory, believing that on the basis of the hydride theory it would be necessary to attribute to such a compound a volume condensation greater than that of the metal and of a higher order than any hitherto observed for compounds or solid solutions. on the other hand the accmrm- lation of transient hydrogen may raise the electrical solution pressure of hydrogen and in general involves no sweeping assumptions as the co-existence of solid solutions and metallic compounds. 18. Summary This work can.not be classed more than a preliminary survey of the adsorpiton of hydrogen'by electrodeposited nickel. The results are considered accurate to within 0.10 cc. at standard conditions. The amount of hydrogen adsorbed on.nickel has been determined at the pB's 5.6, 2.8, 1.7, and at the current densities l, 3, 5, 7, 9, amperes per square decimeter. '1‘! b ' Ik - 9 .. 1 a... '- I‘. 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