US1886411A - Art of removing lead from ferrous articles - Google Patents
Art of removing lead from ferrous articles Download PDFInfo
- Publication number
- US1886411A US1886411A US351131A US35113129A US1886411A US 1886411 A US1886411 A US 1886411A US 351131 A US351131 A US 351131A US 35113129 A US35113129 A US 35113129A US 1886411 A US1886411 A US 1886411A
- Authority
- US
- United States
- Prior art keywords
- lead
- deleading
- solution
- catalyst
- approximately
- 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
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 title description 12
- 239000000243 solution Substances 0.000 description 22
- 150000002815 nickel Chemical class 0.000 description 19
- 239000003054 catalyst Substances 0.000 description 16
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 13
- 239000002253 acid Substances 0.000 description 11
- 229910052500 inorganic mineral Inorganic materials 0.000 description 10
- 235000010755 mineral Nutrition 0.000 description 10
- 239000011707 mineral Substances 0.000 description 10
- -1 hydrogen ions Chemical class 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 235000002639 sodium chloride Nutrition 0.000 description 9
- 150000001805 chlorine compounds Chemical class 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 8
- 230000001590 oxidative effect Effects 0.000 description 8
- 239000011780 sodium chloride Substances 0.000 description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000001117 sulphuric acid Substances 0.000 description 4
- 235000011149 sulphuric acid Nutrition 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000012670 alkaline solution Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 229910000978 Pb alloy Inorganic materials 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- HEPLMSKRHVKCAQ-UHFFFAOYSA-N lead nickel Chemical compound [Ni].[Pb] HEPLMSKRHVKCAQ-UHFFFAOYSA-N 0.000 description 1
- HWSZZLVAJGOAAY-UHFFFAOYSA-L lead(II) chloride Chemical class Cl[Pb]Cl HWSZZLVAJGOAAY-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910001453 nickel ion Inorganic materials 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F1/00—Etching metallic material by chemical means
- C23F1/44—Compositions for etching metallic material from a metallic material substrate of different composition
Definitions
- My invention relates to the art of removing coatings of lead or lead alloys from tubes or other ferrous articles, such as tere plate, scrap, rods, wire, etc.
- the invention consists in removing the lead coating by subjecting the art cle (as by immersion) to a solution contain ng appreciable amounts of chlorides and hydrogen ions resulting from the use of a nonoxidizing mineral acid with a small amount of a catalytic material such as nickel, salts; for example, chloride or sulphate of mckel.
- a catalytic material such as nickel, salts; for example, chloride or sulphate of mckel.
- Lead is one of the best known metals entployed as a material of construction for corrosion resistance. Its use in the manufacture of sulphuric acid and in the chemical mdustries is well known. It is quite resistant to many forms of chemical attack.
- the invention aims to remove lead or lead alloys from articles by subjecting them to a solution which attacks and removes or enables the removal of the lead without considerable or objectionable attack upon the ferrous article.
- a catalyst such referred to materially expedites or speeds up the reaction upon the lead coating and thus by reducing the time of sub ect1on of the article to the deleading bath, reduces the corrosion effect upon the main body of the article.
- the tubes or other articles to be deleaded are first cleaned in an alkaline solution, such as sodium hydroxide, at a temperature preferably near the boiling point; or heated aqueous solutions of so-called commercial cleaners may be employed, or alkali solutions with emulsifying agents such as sulphonated 011s, and various detergents (as sodium carbonate, phos hates, etc.) e
- an alkaline solution such as sodium hydroxide
- the 2111710168 are immersed in the deleading solution in the same general manner or method which is employed in pickling rolled or drawn steel articles.
- a preferred deleading solution comprises appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid.
- a catalyst such as nickel salts
- Sodium chloride in concen trations from about 15% of weight up to saturation, acidified by approximately 5% sulphuric acid, and as a catalyst, a nickel salt, such as chloride or sulphate or nickel, in concentrations from as low as one one-thousandth stituted for the sulphuric acid, the sulphuric being preferred in commercial work because it is a cheaper reagent.
- a nickel salt such as chloride or sulphate or nickel
- the solution shall Work upon and remove the lead without marked effect on the ferrous metal or alloy composing the main bulk of the fabricated article.
- the addition of nickel salts to the bath has been found markedly to speed up the reaction, and thus to reduce attack up on the ferrous body.
- the bath is desirably maintained at a temperature from 180 F. up to the boiling point of the solution.
- the articles After removal from the deleading bath the articles are washed, preferably in hot water, to dissolve and wash off any lead chloride or lead salts still adhering.
- the time-required for deleading is a function of the size of the article, the thickness of the coating, and the surface finish desired.
- Soluble platinum salts may be used in low concentrations in place of nickel salts, but are usually unavailable for this purpose because of the higher cost. Accordingly, wherever I refer in the claims the catalyst, I mean any material which is substantially the equivalent of nickel salts in the sense that it will bring about to a practical-extent the results herein attributed to the presence of nickel salts. It is believed to nickel salts as ing appreciable amounts that the catalytic action of the nickel salt is as follows The nickel ions are precipitated as nickel atoms on the surface of the lead to form a nickel lead electrolytic couple, as the result of which the attack on the lead and its resultant solution is accelerated.
- the present invention is an improvement upon that disclosed in my prior application, Serial No. 325,643, filed December 12, 1928, and consists largely in the addition to certain typical deleading solutions therein disclosed, of a catalyst of the character and for the purposes above described.
- a deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst.
- a deleading process including as a. characteristic operation subjecting a lead coated ferrous article to a solution comprising sodium chloride in concentrations from approximately 15% by weight up to saturation, and approximately 5% non-oxidlzing mineral acid, and a nickel salt as a catalyst in concentrations from approximately 1000th of 1% to approximately of 1%.
- a deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to asolution comprissulphuric acid, and a nickel salt of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small roportion of a nickel salt as a catalyst, the ath being maintained at a temperature near boilmg.
- a deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst, the bath being maintained at a temperature from approximately 180 F. to boiling.
- a deleading process including as a characteristic operation subjecting a lead coated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst, the bath being maintained at a temperature near boilin 11.
- the described process including as characteristic features, cleaning lead-coated ferrous articles in an alkaline solution, subjecting them to a deleading bath of character described in claim 1, and washing the articles to remove remaining lead and deleading solution.
Landscapes
- 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)
- Catalysts (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
. as above Patented Nov.
UNITED STATES OHARLIN L. MANTELL, OF BROOKLYN NEW YORK, ASSIGNOR T0 DUDZEELE CORPORA- TION OF AMERICA, OF NEW YORK, N. Y., A CORPORATION OF DELAWARE ART OF BEHOVING LEAD FROM FERBOUS ARTICLES 80 Drawing. Application filed March 29, 1929, Serial No. 351,131.
My invention relates to the art of removing coatings of lead or lead alloys from tubes or other ferrous articles, such as tere plate, scrap, rods, wire, etc.
Broadly, the invention consists in removing the lead coating by subjecting the art cle (as by immersion) to a solution contain ng appreciable amounts of chlorides and hydrogen ions resulting from the use of a nonoxidizing mineral acid with a small amount of a catalytic material such as nickel, salts; for example, chloride or sulphate of mckel.
Lead is one of the best known metals entployed as a material of construction for corrosion resistance. Its use in the manufacture of sulphuric acid and in the chemical mdustries is well known. It is quite resistant to many forms of chemical attack. The invention aims to remove lead or lead alloys from articles by subjecting them to a solution which attacks and removes or enables the removal of the lead without considerable or objectionable attack upon the ferrous article. The employment of a catalyst such referred to materially expedites or speeds up the reaction upon the lead coating and thus by reducing the time of sub ect1on of the article to the deleading bath, reduces the corrosion effect upon the main body of the article.
In carrying out the process in one approved way, the tubes or other articles to be deleaded are first cleaned in an alkaline solution, such as sodium hydroxide, at a temperature preferably near the boiling point; or heated aqueous solutions of so-called commercial cleaners may be employed, or alkali solutions with emulsifying agents such as sulphonated 011s, and various detergents (as sodium carbonate, phos hates, etc.) e
Af fier cleaning, the 2111710168 are immersed in the deleading solution in the same general manner or method which is employed in pickling rolled or drawn steel articles.
A preferred deleading solution, as generally described, comprises appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid.
with a small amount of a catalyst, such as nickel salts,
or equivalent.
Renewed March 14, 1932.
As a specific example of one approved solution, t 0 following ingredients and proportions are stated:
Sodium chloride (common salt) in concen trations from about 15% of weight up to saturation, acidified by approximately 5% sulphuric acid, and as a catalyst, a nickel salt, such as chloride or sulphate or nickel, in concentrations from as low as one one-thousandth stituted for the sulphuric acid, the sulphuric being preferred in commercial work because it is a cheaper reagent.
In plant operation it is desired that the solution shall Work upon and remove the lead without marked effect on the ferrous metal or alloy composing the main bulk of the fabricated article. The addition of nickel salts to the bath has been found markedly to speed up the reaction, and thus to reduce attack up on the ferrous body. The bath is desirably maintained at a temperature from 180 F. up to the boiling point of the solution.
After removal from the deleading bath the articles are washed, preferably in hot water, to dissolve and wash off any lead chloride or lead salts still adhering.
The time-required for deleading is a function of the size of the article, the thickness of the coating, and the surface finish desired.
Soluble platinum salts may be used in low concentrations in place of nickel salts, but are usually unavailable for this purpose because of the higher cost. Accordingly, wherever I refer in the claims the catalyst, I mean any material which is substantially the equivalent of nickel salts in the sense that it will bring about to a practical-extent the results herein attributed to the presence of nickel salts. It is believed to nickel salts as ing appreciable amounts that the catalytic action of the nickel salt is as follows The nickel ions are precipitated as nickel atoms on the surface of the lead to form a nickel lead electrolytic couple, as the result of which the attack on the lead and its resultant solution is accelerated.
The present invention is an improvement upon that disclosed in my prior application, Serial No. 325,643, filed December 12, 1928, and consists largely in the addition to certain typical deleading solutions therein disclosed, of a catalyst of the character and for the purposes above described.
I claim:
1. A deleading solution containing appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst.
2. A deleading solution containing sodium chloride in concentrations from approxmate- 1y 15% by weight up to saturation, and approximately 5% non-oxidizing mineral acid, and a nickel salt as a catalyst in concentrations from approximately 1000th of 1% to approximately of 1%.
3. A deleading solution containing sodium chloride concentrations from approximately 15 by weight up to saturation, and approximately 5% as a catalyst in concentrations from approxirpagly 1000th of 1% to approximately 0 1 o.
4. A deleading solution containing sodium chloride in concentrations from approximately 15% by weight up to saturation, and approximately 5 non-oxidizing mineral acid, and a nickel salt in small percentage as a catalyst.
5. A deleading solution containing sodium chloride concentrations from approximately 15% by weight up to saturation, and approximately 5% sulphuric acid, and a nickel salt in relatively low concentration as a catalyst.
6. A deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst.
7 A deleading process including as a. characteristic operation subjecting a lead coated ferrous article to a solution compris ing sodium chloride in concentrations from approximately 15% by weight up to saturation, and approximately 5% non-oxidlzing mineral acid, and a nickel salt as a catalyst in concentrations from approximately 1000th of 1% to approximately of 1%.
8. A deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to asolution comprissulphuric acid, and a nickel salt of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small roportion of a nickel salt as a catalyst, the ath being maintained at a temperature near boilmg.
9. A deleading process including, as a characteristic operation, subjecting a leadcoated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst, the bath being maintained at a temperature from approximately 180 F. to boiling.
10. A deleading process including as a characteristic operation subjecting a lead coated ferrous article to a solution comprising appreciable amounts of chlorides and hydrogen ions resulting from the use of a non-oxidizing mineral acid, with a small proportion of a nickel salt as a catalyst, the bath being maintained at a temperature near boilin 11. The described process, including as characteristic features, cleaning lead-coated ferrous articles in an alkaline solution, subjecting them to a deleading bath of character described in claim 1, and washing the articles to remove remaining lead and deleading solution.
12. The described process including as characteristic features, cleaning lead-coated ferrous articles in an alkaline solution, subjectin them to a deleading bath of character descri ed in claim 2, and washing the articles to remove remaining lead and deleading solution.
13. A deleading solution containing appreciable amounts of chlorides and hydrogen ions, with nickel salt as a catalyst.
In testimony whereof I aflix my s 'i%ature.
CHARLES L. MAN LL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US351131A US1886411A (en) | 1929-03-29 | 1929-03-29 | Art of removing lead from ferrous articles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US351131A US1886411A (en) | 1929-03-29 | 1929-03-29 | Art of removing lead from ferrous articles |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1886411A true US1886411A (en) | 1932-11-08 |
Family
ID=23379699
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US351131A Expired - Lifetime US1886411A (en) | 1929-03-29 | 1929-03-29 | Art of removing lead from ferrous articles |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1886411A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2806784A (en) * | 1952-02-19 | 1957-09-17 | Martiny Jean Raymond Valere | Process for wet-refining non-ferrous metals and metal alloys |
| US3112277A (en) * | 1960-09-19 | 1963-11-26 | Universal Oil Prod Co | Regenerating catalysts exposed to contact with plumbiferous waste products |
-
1929
- 1929-03-29 US US351131A patent/US1886411A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2806784A (en) * | 1952-02-19 | 1957-09-17 | Martiny Jean Raymond Valere | Process for wet-refining non-ferrous metals and metal alloys |
| US3112277A (en) * | 1960-09-19 | 1963-11-26 | Universal Oil Prod Co | Regenerating catalysts exposed to contact with plumbiferous waste products |
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