Classifications

• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
  • C25F3/00—Electrolytic etching or polishing
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
  • B23H—WORKING OF METAL BY THE ACTION OF A HIGH CONCENTRATION OF ELECTRIC CURRENT ON A WORKPIECE USING AN ELECTRODE WHICH TAKES THE PLACE OF A TOOL; SUCH WORKING COMBINED WITH OTHER FORMS OF WORKING OF METAL
  • B23H3/00—Electrochemical machining, i.e. removing metal by passing current between an electrode and a workpiece in the presence of an electrolyte
  • B23H3/08—Working media

Definitions

• the hexavalent chromium content of aqueous chlorate-containing electrolyte solution employed in electrochemical machining or grinding operations may be reduced through reduction to the trivalent chromium state from which it will precipitate as hydrous chromic oxide or by removal in the hexavalent state by precipitation as a barium, lead, zinc, cobalt or copper salt.
• the removal of trace hexavalent chromium values from a chlorate-containing electrochemical machining electrolytic solution reduces the fire hazard attending the use of chlorate-containing solutions which may accidentally wet an organic material such as an operator's clothing and subsequently dry to form an extremely combustible mixture.
• E- Alkali metal and ammonium chlorates, especially sodium chlorate are ideal electrolytes for use in electrochemical machining operations.
• the major problem attending their use resides in their tendency to rapidly oxidize combustible materials.
• the advantages and problems residing in the use of chlorates as the electrolyte in electrochemical machining operations are summarized in the article appearing in Metal Progress, March 1967, pp. 81-84. For example, when some of the chlorate-containing electrolyte comes into contact with the clothing of the operator, or any combustible material near an electrochemical machining operation, the tendency to initiate tire is great after the wetted material has dried.
• electrochemical machining operations it is intended to include those operations by which a workpiece is machined, milled, or ground so that the metal is removed by an electrochemical process to produce shaped or curved structures.
• electrochemical processes by which a hole is bored into or through a workpiece or the surface of a workpiece is smoothed is embraced by the expression electrochemical machining operations.
• the workpiece to be shaped functions as the anode in electrically conducting rela tionship with the cathode die through a suitable electrolyte.
• Electrochemical machining or grinding embraces those procedures which employ a metal or metalloid material as a workpiece from which material is to be removed via electrolytic attack.
• the workpiece is the anode while the die or grinding wheel is connected as the cathode and the electrical circuit is completed from anode to cathode by the electrolyte (alkali metal or ammonium chlorate).
• the electrolyte may be directed into the work gap through the cathode if a hollow electrode is employed or the electrolyte may be presented to the work gap by any means known to the art.
• the solution of electrolyte is held in a reservoir from which it may be fed to the work gap and back to the holding reservoir. Sludge which forms in the electrolyte solution will slowly settle out in the holding reservoir yielding a thickened slurry which way be removed by filtration.
• Sodium chlorate is an excellent electrolyte for electrochemical machining operations.
• Sodium chlorate solutions used as the electrolyte in electrochemical machining are typically aqueous solutions containing about 350 grams per liter Na,Cl0
• a typical solution is one containing 3 pounds of sodium chlorate per gallon, which is equal to 359 grams per liter.
• a typical electrochemical machining electrolyte may be considered to be an aqueous solution containing from about 300 to 400 grams sodium chlorate per liter.
• the used electrolyte solutions usually of pH above about 6 to 7, contain precipitated hydroxides of the metal removed from the workpiece. For example, where the workpiece contains iron, nickel or chromium, the corresponding iron, nickel or chromium hydroxides are formed.
• the burning time for untreated cloth is about 36 seconds
• the bu'ming time for the cor responding cloth which has bee dried after impregnation with about 1 gram of sodium chlorate solution per gram of cloth under conditions of controlled humidity at room temperature, will vary from about 6 seconds to about 12.6 seconds, based upon the relative humidity of the drying atmosphere of 20 percent for the former and about 52 percent for the latter.
• the buming time for the test cloth dried at 20 percent relative humidity will increase to 4.1 seconds at 0.05 gram Cr per liter; to 3.2 seconds at 0.1 gram Cr per liter; to L9 seconds at from 0.5 to 2.0 grams Cr per liter.
• flame-retardant additives may be included with an alkali metal or ammonium chlorate as the electrolyte solution in electrochemical machining and grinding operations.
• the flame-retardant additives such as sodium metasilicate and sodium hydroxide greatly reduce the burning time of cotton cloth which has been wetted with a chlorate-containing solution and subsequently dried.
• this flame-retarding influence is somewhat diminished when hexavalent chromium is introduced into the electrolyte solution form oxidized chromium metal found in alloys machined by electrochemical techniques.
• the hexavalent chromium ion content which is introduced into the aqueous sodium chlorate electrolyte solution employed to electrochemically machine a metal alloy containing chromium by oxidation of the chromium metal to the hexavalent chromium state (e.g.
• Coll may be removed by the regular addition of a reducing agent such as an alkali metal or ammonium sulfide, stannous salts such as SnS0.,, SnCl and the ferrous salts such as FeSO FeCll and Fc(I lt') to the chlorate-chromatc-containing solution to reduce the chromate ion to the trivalent chromium valence state in which state the chromium precipitates from solution as hydrous chromic oxide.
• the reducing agent must not react with the alkali metal or ammonium chlorate in the aqueous solution under the electrolytic conditions employed (i.e. above pH 6 with from about 300 to 400 grams NaClltl per liter).
• An especially applicable and the preferred reducing agent is the ferrous Fe) ion, added to the hexavalent chromium-ioncontaining solution as a soluble salt, such as the chloride, sulfate or nitrate.
• a soluble salt such as the chloride, sulfate or nitrate.
• An alkali may be added in combination with the ferrous salt to prevent acidification of the electrolyte solution through formation of HCl, H 30 etc. coming from the ferrous salt.
• the overall reaction involved in this process taking place in aqueous solution may be noted as:
• n and 2 vary with conditions of the precipitation.
• the hydrous oxides of i-e and Cr thus formed are the same type of compound as the metal hydroxides or hydrous oxides comprising the sludge normally encountered in electrochemical machining operations and the Cr,0 .xll-H O does not noticeably accelerate the burning of cloth when wetted with the chlorate solution, dried and ignited.
• the hydrous oxides of Fe" and Cr may then be removed from the electrolytic solution along with the sludge derived from the metal coming from the machining of the workpiece by filtration or some other applicable procedure known to the art. After this treatment, only a few parts per million of hexavalent chromium ions remain dissolved in the electrolyte.
• a reducing agent to the hexavalent chromium-containing electrolyte may be made at any stage of an electrochemical machining operation.
• the hydrous chromium oxide and hydrous iron oxide will remain in suspension in the aqueous electrolyte along with the metal hydroxides or hydrous oxides formed during the machining operation until they are removed by known methods such as filtration.
• the reducing agent may be well mixed with the electrolyte to afford the optimum reduction of hexavalent chromium. By this procedure, the hexavalent chromium level may be maintained at a very low level in the chlorate electrolyte solution.
• the chromate ions may be removed through precipitation of an insoluble chromate salt.
• the aqueous chlorate-containing electrolyte solution which has been contaminated by Cr ions may be treated with a small excess of the required stoichiometric amount of a soluble salt containing a member selected from the group consisting of divalent barium, lead, zinc, cobalt and copper.
• the anions forming soluble salts with these cations are for example the chlorides, nitrates, etc.
• reagents already formulated into an aqueous solution as a nitrate and introduce the reagent in the electrolyte solution just prior to sludge removal so that the BaCrO.,, CoCr0.,, Pb- CrO ZnCro, or CuCrOrCuO precipitate may be removed with the sludge.
• EXAMPLE I The burning time for cloth impregnated with unused electrolyte solution containing 400 grams NaClltl per liter and no hexavalent chromium was 6.0 seconds. After this electrolyte was used in electrochemical grinding of 304 stainless steel containing about ZO-percent chromium, the chromate concentration of the aqueous electrolyte was about 0.5 gram of chromium per liter and the burning time for cloth impregnated with the resulting solution was 4.1 seconds. When the chromium content of the used electrolyte rose to 0.1 gram per liter the burning time was 3.2 seconds; at 0.5 gram chromium per liter a burning time of L9 second was observed.
• EXAMPLE ll An electrolyte containing 400 grams NaCiiti per liter and 12 grams NaOll-i per liter as a flame retardant was employed as the electrolytic solution for an electrochemical grinding operation.
• the resulting solution contained 0.l gram chromium per liter as CrOJ and resulted in a cloth-blaming time of 12.5 seconds.
• To 1 liter of the used solution was added 20 milliliters of an aqueous solution containing 0.97 gram FeSO, l 10 percent of theory) and 10 milliliters of an aqueous solution containing 0.34 gram of NaOh. After removal of the precipitate, the chlorate-containing solution retained less than 10 parts per million of chromium and gave a burning time of 70 seconds.
• EXAMPLE ill An electrolyte solution of 400 grams NaCiti, per liter and 51 grams per liter of Na- SiO as flame retardant was used for electrochemical grinding as in example ii. The final liquid phase acquired 0.5 gram chromium per liter as soluble chromate. As in example ll, solutions containing 4.85 grams of FeSo, and 1.7 grams of NaOH were added simultaneously but separately. The treated liquid contained less than 10 parts per million chromium and resulted in a cloth-burning time of 250 seconds as compared to a burning time 6.9 seconds for the solution prior to chromium removal when ignited with a 4- inch gas flame (large source).
• reducing agents other then ferrous salts may be employed to convert hexavalent chromium ions to the trivalent state.
• any reducing agent may be employed that does not reduce the sodium chlorate or any flameretardant additive present in the electrolyte.
• other means for removing hexavalent chromium from the aqueous chlorate-containing solution may be used such as various inorganic salts which form insoluble chromates. Therefore, the examples herein presented are intended to be illustrative of the inventive concepts rather than limitations upon the actual scope of this contribution.
• the improvement which comprises reducing organic material combustibility by removing hexavalent chromium ions from said aqueous chlorate-containing solution by introducing into said solution at least one member selected from the group consisting of the soluble salts of divalent Fe, Sn, Ba, CO, Pb, Zn, Cu, an alkali metal sulfide and ammonium sulfide and removing the precipitate.

Landscapes

• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
• Chemical Treatment Of Metals (AREA)

Applications Claiming Priority (1)

Publications (1)

Family

ID=24801741

Family Applications (1)

Country Status (6)

Cited By (9)

Families Citing this family (2)

• 1968
  • 1968-01-15 US US697595A patent/US3616344A/en not_active Expired - Lifetime
• 1969
  • 1969-01-02 GB GB1252691D patent/GB1252691A/en not_active Expired
  • 1969-01-09 DE DE19691900996 patent/DE1900996A1/de active Pending
  • 1969-01-13 BE BE726812A patent/BE726812A/fr unknown
  • 1969-01-14 FR FR6900424A patent/FR2000237A1/fr not_active Withdrawn
  • 1969-01-15 NL NL6900681A patent/NL6900681A/xx unknown

Also Published As

Similar Documents

Legal Events