US1592935A - Process of recovering tin - Google Patents

Process of recovering tin Download PDF

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Publication number
US1592935A
US1592935A US2652425A US1592935A US 1592935 A US1592935 A US 1592935A US 2652425 A US2652425 A US 2652425A US 1592935 A US1592935 A US 1592935A
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Prior art keywords
tin
scrap
recovering
ammonia
sodium
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Elmo G Hickey
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Individual
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Priority to US2652425 priority Critical patent/US1592935A/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B25/00Obtaining tin
    • C22B25/06Obtaining tin from scrap, especially tin scrap
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • This invention relates to process for recovering tin from tin cans, scrap tin and other tin surfaces.
  • An object of this invention is to provide a process by which the tin may be recovered from tin scrap, refuse, tin cans, and the like, in a relatively short time, maintaining a high efliciency of the recovery of the tin.
  • the tin scrap, tin cans, and the like, properly cleaned and perforated is sub-- jected to the action of a solution of caustic soda and sodium nitrate to which from .3% to 3% by weight of ammonium hydroxide has been added; the ammonium hydroxide used being approximately 28% NH
  • the solution is heated approximately to boiling. This solution is from 4 to 12% sodium nitrate and from 18 to 28% sodium hydroxide, although it is to be understood that other alkali-metal hydroxides might be employed Application filed April as, 1925. Serial No. 26,524.
  • nitrates other than sodium nitrate mlght be employed in this process with equal elficiency, sodium nitrate and sodium hy- "covered that the tin will be completely removed from the tin scrap within approximately an hour, where heretofore it has required from 6 to 7 hours to obtain the same tin recovery.
  • this invention relates tovthe use of ammonia as a catalytic agent for accelerating the rate of recovery of tin from tin scrap and that the same is in no way dependent upon the percentages of sodium hydroxides and sodium nitrate employed other than that the same should be of suflicient strength to remove the tin from the tin bearing scrap and precipitate the same, preferably as sodium stannate.
  • a process of recovering tin from tin scraps which comprises subjecting the tin scraps to the action of caustic alkali and alkali metal nitrate in the presence of ammonia.
  • a process of recovering tin from tin scraps comprising subjecting tin scrap to the action of caustic alkali and alkali "metal nitrate in the presence of from .3 to 3% of ammonia hydroxide containing 28% ammonia by weight.
  • V 3 In a process of recovering tin from tin scraps, employing caustic alkali solution, the step which includes the use of ammonia as an energizing agent.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Processing Of Solid Wastes (AREA)

Description

Patented July 20, 1926. i I
ELMO G. HICKEY, OF LOS ANGELES, CALIFORNIA.
PROCESS OF RECOVERING TIN.
Io Drawing.
This invention relates to process for recovering tin from tin cans, scrap tin and other tin surfaces.
For approximately the past fifty years various processes for the removal of tin from tin bearing scrap, tin cans and the like, have been known and used. These processes have, for the most part, been based upon the fact that tin is soluble in either hot or cold solutions of caustic alkali in the presence of alkali metal nitrates. These processes have, for the most part, a number of difiiculties, one of which difficulties has been in thedevelopment of this recovery process from the standpoint of com-.
mercial success because of the relatively long time required for this action to take place and the consequent excessive high cost in plant expense, handling charges of any considerable quantity of material to be detinned, such as tin scrap, refuse, tin cans, and the like.
An object of this invention is to provide a process by which the tin may be recovered from tin scrap, refuse, tin cans, and the like, in a relatively short time, maintaining a high efliciency of the recovery of the tin.
I have discovered that the recovery of tin is greatly accelerated by ,the addition of ammonia to the alkaline solution composed of caustic soda and alkaline nitrates. According to the preferred form of the invention, the tin scrap, tin cans, and the like, properly cleaned and perforated, is sub-- jected to the action of a solution of caustic soda and sodium nitrate to which from .3% to 3% by weight of ammonium hydroxide has been added; the ammonium hydroxide used being approximately 28% NH The solution is heated approximately to boiling. This solution is from 4 to 12% sodium nitrate and from 18 to 28% sodium hydroxide, although it is to be understood that other alkali-metal hydroxides might be employed Application filed April as, 1925. Serial No. 26,524.
and that nitrates other than sodium nitrate mlght be employed in this process with equal elficiency, sodium nitrate and sodium hy- "covered that the tin will be completely removed from the tin scrap within approximately an hour, where heretofore it has required from 6 to 7 hours to obtain the same tin recovery.
Having fully described the preferred embodiment of this invention, it is to be under,- stood that this invention relates tovthe use of ammonia as a catalytic agent for accelerating the rate of recovery of tin from tin scrap and that the same is in no way dependent upon the percentages of sodium hydroxides and sodium nitrate employed other than that the same should be of suflicient strength to remove the tin from the tin bearing scrap and precipitate the same, preferably as sodium stannate.
I claim:
1. A process of recovering tin from tin scraps which comprises subjecting the tin scraps to the action of caustic alkali and alkali metal nitrate in the presence of ammonia.
2. A process of recovering tin from tin scraps comprising subjecting tin scrap to the action of caustic alkali and alkali "metal nitrate in the presence of from .3 to 3% of ammonia hydroxide containing 28% ammonia by weight. V 3. In a process of recovering tin from tin scraps, employing caustic alkali solution, the step which includes the use of ammonia as an energizing agent.
Signed at Los Angeles, California, this 23d day of April 1925.
ELMO G. HICKEY.
US2652425 1925-04-28 1925-04-28 Process of recovering tin Expired - Lifetime US1592935A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US2652425 US1592935A (en) 1925-04-28 1925-04-28 Process of recovering tin

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Application Number Priority Date Filing Date Title
US2652425 US1592935A (en) 1925-04-28 1925-04-28 Process of recovering tin

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US1592935A true US1592935A (en) 1926-07-20

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4164542A (en) * 1973-05-08 1979-08-14 Pincus Deren Detinning process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4164542A (en) * 1973-05-08 1979-08-14 Pincus Deren Detinning process

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