US1269443A - Pickling process and bath. - Google Patents
Pickling process and bath. Download PDFInfo
- Publication number
- US1269443A US1269443A US20140217A US20140217A US1269443A US 1269443 A US1269443 A US 1269443A US 20140217 A US20140217 A US 20140217A US 20140217 A US20140217 A US 20140217A US 1269443 A US1269443 A US 1269443A
- Authority
- US
- United States
- Prior art keywords
- bath
- pickling
- ferric
- solution
- manganese
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000005554 pickling Methods 0.000 title description 18
- 238000000034 method Methods 0.000 title description 13
- 150000003839 salts Chemical class 0.000 description 11
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 230000003647 oxidation Effects 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical class [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 150000002697 manganese compounds Chemical class 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 230000001706 oxygenating effect Effects 0.000 description 3
- 235000021110 pickles Nutrition 0.000 description 3
- GOPYZMJAIPBUGX-UHFFFAOYSA-N [O-2].[O-2].[Mn+4] Chemical compound [O-2].[O-2].[Mn+4] GOPYZMJAIPBUGX-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 2
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 2
- 150000002696 manganese Chemical class 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 241000270281 Coluber constrictor Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 241001237728 Precis Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000008135 aqueous vehicle Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- OQZCSNDVOWYALR-UHFFFAOYSA-N flurochloridone Chemical compound FC(F)(F)C1=CC=CC(N2C(C(Cl)C(CCl)C2)=O)=C1 OQZCSNDVOWYALR-UHFFFAOYSA-N 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 229940099596 manganese sulfate Drugs 0.000 description 1
- 235000007079 manganese sulphate Nutrition 0.000 description 1
- 239000011702 manganese sulphate Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/36—Regeneration of waste pickling liquors
Definitions
- the present invention relates to a pickling process and bath used therein, and particular reference to that type of processes in which the bath or pickle liquor, after being used for treating the iron or steel articles, or similar articles to be pickled, is revivified by being subjected to an oxidation treat ment, whereby the ferrous salts therein are either partially or entirely converted into ferric salts, as in my prior Patent 1,146,071.
- lean employ either dilute sulfuric acid or dilute muriatic acid, or in some cases a solution of niter' cake or other acid salt.
- the iron article is pickled in this solution in the usual manner, after which it is preferred to withdraw the pickle liquor, when the same has nocumulated a considerable quantity of ferrous sulfate" or other ferroussalts.
- this ll add manganesedioxid or a salt of man anese such as manganese sulfate, or chlorld, and I then oxidize the liquor, which can be conveniently done as in my prior patent, namely by allowing the same to trickle down through a tower against a counter current of air oroxygen or other omdizing gas.
- the manganese compounds can be .added at any desired stage of the process.
- the precipitated material may; contain a considerable amount of the total amount of manganese compounds present, either manganese dioxid (hydrated) or compounds of ln some instances it is not necessaryto withdraw the waste pickle liquor from the pickling tank, but the liquor may be treated in the tank in which the pickling operation has been carried out, with the addition of a catalyzing agent such as the manganese salts above referred to, by oxidation, the ferrous salt in solution being oxidized.
- the step of oxidizing the ferrous to ferric salt, by the action of air or other oxidizing gas it is preferable to maintain the solution at or near its boiling point, under which conditions a considerably larger quantity of ferric hydrate or partially hydrated ferric oxid will be precipitated than 7 would occur at ordinary room temperature,
- the pickling process is started with an acid liquor, but after the formation of ferric salts, the pickling is also in part edected by the chemical action of the said ferric salt.
- the solution, when in contact with ferrous articles bemg pickled is preferably maintained at a temperature of about 100 (C,
- an oxygenating catalyst This term is well understood in the art of catalysis to refer to ,such catalysts as promote reactions in which oxygen (such as free oxygen contained in air) is caused to react with other materials.
- a pickling bath comprising an aqueous vehicle containing sulfuric acid, ferric sulfate, and a manganese salt.
- process of pickling which comprises subjecting the article to be pickled to the action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation in the presence of a catalyzer.
- a process of picklin which comprises subjecting .the artlcle to %e pickled to the action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation by treating the same with an oxidizing agent in the presence of a catalyzer, while the solution is at a boiling temperature.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Catalysts (AREA)
Description
hurra snares rand onruon.
ADDISON F. HOFFMAN, F PITTSBURGH, PENNSYLVANIA.
PIIUKIIING PROCESS A'hl'D BATH.
nee les.
upcctficatiers racer. Patented dune til, wild We Drawing. deputation filed January as, 1917, Serial No. ieaooi. Renewed November 10, 191?. serial lilo. 201M322.
To all whom it may concern: I
Be it known that l, Anorson F. HOFFMAN, a citizen of the United States, residing at Pittsburgh, in the county of Alleghen and State of Pennsylvania, have invente new and useful Improvements in Pickling Processes and Baths, of which the following is a specification.
The present invention relates to a pickling process and bath used therein, and particular reference to that type of processes in which the bath or pickle liquor, after being used for treating the iron or steel articles, or similar articles to be pickled, is revivified by being subjected to an oxidation treat ment, whereby the ferrous salts therein are either partially or entirely converted into ferric salts, as in my prior Patent 1,146,071.
In operating the process of my prior patent referred to, l have found that the oxidation of the ferrous salts to ferric salts is in some instances rather difiicult, particularly when the liquor is rather strongly impregnated with ferrous compounds. however, found that this objection can be overcome by addition to the liquid of a suitable catalytic or other agent, of which class of bodies manganese compounds have been found to give excellent results in practice.
As the starting material for the bath for pickling iron and the like, lean employ either dilute sulfuric acid or dilute muriatic acid, or in some cases a solution of niter' cake or other acid salt. The iron article is pickled in this solution in the usual manner, after which it is preferred to withdraw the pickle liquor, when the same has nocumulated a considerable quantity of ferrous sulfate" or other ferroussalts. llo this ll add manganesedioxid or a salt of man anese such as manganese sulfate, or chlorld, and I then oxidize the liquor, which can be conveniently done as in my prior patent, namely by allowing the same to trickle down through a tower against a counter current of air oroxygen or other omdizing gas. The manganese compounds can be .added at any desired stage of the process.
In some cases it is feasible to employ ozonized air for this step. Theomdation in many cases will convert a considerable portion of the ferrous salts in solution into ferric sulfate which when acted upon by heat in the presence of water is in part hydrolyzecl, prod i g ferric hydr uid c m l have,
pounds or perhaps basic ferric salts which are precipitated and can be removed from the bath before adding a further amount of sulfuric acid and bringing the same back into the pickling tank. ln some instances the precipitated material may; contain a considerable amount of the total amount of manganese compounds present, either manganese dioxid (hydrated) or compounds of ln some instances it is not necessaryto withdraw the waste pickle liquor from the pickling tank, but the liquor may be treated in the tank in which the pickling operation has been carried out, with the addition of a catalyzing agent such as the manganese salts above referred to, by oxidation, the ferrous salt in solution being oxidized. x
In 'he oxidation of the solution by oxygen from any source, a considerable portion of the iron in solution may be preci itated, which by calcination yields an excel ent variety of ferric oxid suitable for use as a pigment or polishing material.
ln the step of oxidizing the ferrous to ferric salt, by the action of air or other oxidizing gas, it is preferable to maintain the solution at or near its boiling point, under which conditions a considerably larger quantity of ferric hydrate or partially hydrated ferric oxid will be precipitated than 7 would occur at ordinary room temperature,
perhaps since the free acid at ordinary room temperature is considerably more active in dissolving basic ferric hydrate, and basic ferric salts, than at or near the boiling point.
The pickling process is started with an acid liquor, but after the formation of ferric salts, the pickling is also in part edected by the chemical action of the said ferric salt. For this purpose, the solution, when in contact with ferrous articles bemg pickled is preferably maintained at a temperature of about 100 (C,
too
In this specification, and in the claims, I have referred to the use of an oxygenating catalyst. This term is well understood in the art of catalysis to refer to ,such catalysts as promote reactions in which oxygen (such as free oxygen contained in air) is caused to react with other materials.
. My experiments show that various compounds of manganese, besides the dioxid, such as the sulfate, chlorid or hydroxid, whether containing the manganese in the form of compounds of MnO or compounds .MnO are suitable for the purpose.
What I claim is: 1. A process of pickling which comprises subjecting the article to be pickled to ,the
action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation by treating the same with an oxidizing agent in the presence of an oziggenating catalyist.
2 process of pickling which comprises sub ecting the art1cle to be pickled to the action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation by treating the same with an oxidizing agent in the presence of a manganese compound capable of serving as an oxygenating catal st.
3. A process of pickli subjecting the article to be pickled to the action of a pickling solution containing a ferric salt and a free acid, and subsequently ng which comprises rjaeaaaa metal articles, said bath comprising an acid solution of a ferric salt, containing'an oxygenating catalyst.
6. A pickling bath comprising an aqueous vehicle containing sulfuric acid, ferric sulfate, and a manganese salt.
75A. process of pickling which comprises subjecting the article to be pickled to the action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation in the presence of a catalyzer.
8. A process of picklin which comprises subjecting .the artlcle to %e pickled to the action of a pickling solution and restoring the bath to an active condition by subjecting the same to oxidation by treating the same with an oxidizing agent in the presence of a catalyzer, while the solution is at a boiling temperature.
In testimonywhereof l atiix my signature.
'- ADDISON F. HOFFMAN.
till
bib
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US20140217A US1269443A (en) | 1917-11-10 | 1917-11-10 | Pickling process and bath. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US20140217A US1269443A (en) | 1917-11-10 | 1917-11-10 | Pickling process and bath. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1269443A true US1269443A (en) | 1918-06-11 |
Family
ID=3337081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US20140217A Expired - Lifetime US1269443A (en) | 1917-11-10 | 1917-11-10 | Pickling process and bath. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1269443A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423385A (en) * | 1944-07-27 | 1947-07-01 | Chemical Foundation Inc | Process of pickling and of recovering pickling agent |
| US2564549A (en) * | 1945-07-02 | 1951-08-14 | Albert R Stargardter | Pickling treatment |
| US3529998A (en) * | 1966-02-16 | 1970-09-22 | Fritz Singer | Pickling process |
| US4389254A (en) * | 1978-10-27 | 1983-06-21 | Centre De Recherches Metallurgiques-Centrum Voor Research In De Metallurgie | Continuous treatment of steel sheet |
-
1917
- 1917-11-10 US US20140217A patent/US1269443A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423385A (en) * | 1944-07-27 | 1947-07-01 | Chemical Foundation Inc | Process of pickling and of recovering pickling agent |
| US2564549A (en) * | 1945-07-02 | 1951-08-14 | Albert R Stargardter | Pickling treatment |
| US3529998A (en) * | 1966-02-16 | 1970-09-22 | Fritz Singer | Pickling process |
| US4389254A (en) * | 1978-10-27 | 1983-06-21 | Centre De Recherches Metallurgiques-Centrum Voor Research In De Metallurgie | Continuous treatment of steel sheet |
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