[go: up one dir, main page]

US1169365A - Manufacture of reduction products of sulfurous acids and salts thereof. - Google Patents

Manufacture of reduction products of sulfurous acids and salts thereof. Download PDF

Info

Publication number
US1169365A
US1169365A US81606314A US1914816063A US1169365A US 1169365 A US1169365 A US 1169365A US 81606314 A US81606314 A US 81606314A US 1914816063 A US1914816063 A US 1914816063A US 1169365 A US1169365 A US 1169365A
Authority
US
United States
Prior art keywords
zinc
formaldehyde
salts
spongy
manufacture
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
Application number
US81606314A
Inventor
Heinrich Specketer
Eduard Marburg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemische Fabrik Griesheim Elektron
Original Assignee
Griesheim Elektron Chem Fab
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Griesheim Elektron Chem Fab filed Critical Griesheim Elektron Chem Fab
Priority to US81606314A priority Critical patent/US1169365A/en
Application granted granted Critical
Publication of US1169365A publication Critical patent/US1169365A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C313/00Sulfinic acids; Sulfenic acids; Halides, esters or anhydrides thereof; Amides of sulfinic or sulfenic acids, i.e. compounds having singly-bound oxygen atoms of sulfinic or sulfenic groups replaced by nitrogen atoms, not being part of nitro or nitroso groups
    • C07C313/02Sulfinic acids; Derivatives thereof
    • C07C313/04Sulfinic acids; Esters thereof

Definitions

  • spongy zinc can be very easil obtained from zincoxid, zinc hydroxid', zinc carbonate, or waste containing oxidizable zinc, and as the oxidized waste resulting from the reduction process can be readily regenerated, spongy zinc is not only much cheaper than zinc dust but has also the advantage that in consequence of its easy recuperation the process can be conducted with a minimum of zinc and the industrial carrying out of the reduction process is'not only simplified and expedited by the end-- ployment of spongy zinc but it is also considerably cheapened, and this is of great importance in the manufacture of reduction products of sulfurous acid, because the price of zinc dust has formed a large item of the total cost of production, even taking into account value of the resulting residues containing ZlIlC oxid.
  • furous acid, and salts thereof may be accounted for by the fact that no industrial advantage was foreseen, and it'was supposed that spongy zinc would not be sufficiently durable.
  • aldehyde sulfoxylate spongy zinc possesses another important, and hithertounknown property for the purpose of the reduction.
  • alkali-bis ullite-formaldehyde or from a formaldehyde sulfite mixture :such as hydrosulfitformah dehyde, i. c.
  • the desired efiect is obtained by the addition'of Zinc-, or ammonium-sulfite,-or -bisulfite, or by the addition of the zinc-, or ammonium'salts of formaldehyde-sulfurous acid, or of formaldehyde-hydrosulfurous zinc hydroxid, or zinc carbonate, more than;
  • Example 1 Sulfurous acid is passed into a quantity of moist electrolytically prepared spongy Zinc containing 100 kilograms of metallic zinc under 300 liters of water, while being well stirred and cooled, until the zinc has for the greater part disappeared.
  • the zinc hydrosulfite solution obtained is decomposed by means of a suitable alkali salt, for instance sodium carbonate, tered. i highly concentrated solution of sodium hydrosulfite is thus obtained.
  • Example 2 152 kilograms ot'sodium bisulfite-formaldehye (NaHSO CILOII O) dissolved in from 200, to 250, kilograms of water are stirred with a quantity of moist electrolytically prepared spongy zinc containing 100 kilograms of metallic. zinc and well boiled for from 1 to 2 hours while being stirred. The solution filtered off from zinc sludge contains from 130 to H0 kilograms of sodium formaldehyde-sultoxylate.
  • the solid salt is obtained.
  • Example 3 A solution of 305 kilograms of sodium hydrosulfite formaldehyde in 850 liters of water is stirred with a quantity of moist spongy zinc, electrolytically prepared and containing 100 kilograms of zinc and boiled for from 1, to 2, hours while stirring.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

ICE SEECKEEJEE Al '3, QJlT-El-IE-MAIN, GERMfiIT I, A
TD EIGUAED MARBURG, G13 GRIESHEZL'lVlI-ON-THE-MAIN, GEE- NY, iiSfiIGNQES T0 GHQ-a ""SCHE FABRIK GR-IESI-IEIM-ELEKT'RON, GT3 FRANKFOBT- CORPORATION OF GERMANY.
IvIANUFAC'EUE-E GE REDUCTION PRODUCTS OF SULFURGUS ACIDS AND SALTS THEREOF.
lie Brewing.
1'10 all whom it may concern:
it known that we, Hammett Senoritaand licence Milanese, both subjects of the GermanEmperor, and resident of Griesheila-onthehlain, Germany, have invented certain new and useful improvements in Connection with the Manufacture of Roi duction roducts of Sulfurous Acid and ployed and the use of spongy zinc in addi-- tion to thus enabling the operation to becarried on much more expeditiously than hitherto )resents the further advanta e' that even with the more rapid supply of sulfurous acid, excessive'acidity and decomposition of the solution of hydrosulfite do not occur.
As spongy zinc can be very easil obtained from zincoxid, zinc hydroxid', zinc carbonate, or waste containing oxidizable zinc, and as the oxidized waste resulting from the reduction process can be readily regenerated, spongy zinc is not only much cheaper than zinc dust but has also the advantage that in consequence of its easy recuperation the process can be conducted with a minimum of zinc and the industrial carrying out of the reduction process is'not only simplified and expedited by the end-- ployment of spongy zinc but it is also considerably cheapened, and this is of great importance in the manufacture of reduction products of sulfurous acid, because the price of zinc dust has formed a large item of the total cost of production, even taking into account value of the resulting residues containing ZlIlC oxid. I
The fact that, although spongy zinc obtained by electrolysis has been long known it has notv been used in place of zinc dust for the production reduction products of end 5 Specification of Letters Patent.
Application filed February 2, 1914. SerialNo. 816,063.
furous acid, and salts thereof may be accounted for by the fact that no industrial advantage was foreseen, and it'was supposed that spongy zinc would not be sufficiently durable.
In the production of aldehyde sulfoxylate spongy zinc possesses another important, and hithertounknown property for the purpose of the reduction. We have found that, by starting from a ready-made alkali-bis ullite-formaldehyde, or from a formaldehyde sulfite mixture :such as hydrosulfitformah dehyde, i. c. a mixture or double salt of bisulfite-formaldehyde and formaldehyde-Sid roxylate, it is possible to readily obtain, without any further addition, an excellent yield of formaldehyde sulfoxylates, if spongy Zinc obtained by electrolysis be used as reducing agent The yield is in this case about 85 ,to 90 per cent. Hitherto it has not been possible to carry out successfully the direct production of the formaldehyde-sulfoxylates by reduction of the ready made alkali-bisulfite formaldehydes or hydrosulfite-formaldehydes by means of zinc dust without the use of considerable quantities of an addition for insuring the favorable run of the reaction; For instance in accordance f with the specification 'ofGerman Patent No. 165,807 an addition of acid (for instance acetic acid) is needed. In accordance with the specification of German Patent No. 222,195, the desired efiect is obtained by the addition'of Zinc-, or ammonium-sulfite,-or -bisulfite, or by the addition of the zinc-, or ammonium'salts of formaldehyde-sulfurous acid, or of formaldehyde-hydrosulfurous zinc hydroxid, or zinc carbonate, more than;
60 per cent. of the full equivalent of zinc paid being added. The same object, namely FT rim he avoidance of an addition of acidand the consequent production of the zinc and alkali salts of this acid, is attained in the process in accordance with thespecification of German Patent No. 20224-2. in which it is proposed to cause sodium bisullite, formaldehyde and zinc dust to react on one another at a full boiling heat. In this case too the addition which is essential for the reaction is the suitably chosen excess or free sodium bisulfite, starting from the ready formed bisulfite formaldehyde 9 being expressely avoided.
As zinc-dust itself is a i'ery energetic and finely dividing reducing agent, it was not to be foreseen that by using electrolytically prepared spongy zinc, it would be possible to give up the use of the additions hitherto employed.
The following are examples of how this invention can be carried into effect, but we do not limit ourselves to these examples.
Example 1: Sulfurous acid is passed into a quantity of moist electrolytically prepared spongy Zinc containing 100 kilograms of metallic zinc under 300 liters of water, while being well stirred and cooled, until the zinc has for the greater part disappeared. The zinc hydrosulfite solution obtained is decomposed by means of a suitable alkali salt, for instance sodium carbonate, tered. i highly concentrated solution of sodium hydrosulfite is thus obtained.
Example 2: 152 kilograms ot'sodium bisulfite-formaldehye (NaHSO CILOII O) dissolved in from 200, to 250, kilograms of water are stirred with a quantity of moist electrolytically prepared spongy zinc containing 100 kilograms of metallic. zinc and well boiled for from 1 to 2 hours while being stirred. The solution filtered off from zinc sludge contains from 130 to H0 kilograms of sodium formaldehyde-sultoxylate. By
evaporating at low temperature preferably in venue, the solid salt is obtained.
. Example 3: A solution of 305 kilograms of sodium hydrosulfite formaldehyde in 850 liters of water is stirred with a quantity of moist spongy zinc, electrolytically prepared and containing 100 kilograms of zinc and boiled for from 1, to 2, hours while stirring.
- messes alkali-hydrosulfite-formaldehyde by spongy zinc to form alkali formaldehydesulfoxylate.
3: The process'of producing hydrosulfurous acid compounds from sulfurous acid compounds which com-prises reducing such sulfurous acid compounds by ,means of spongy Zinc. i 4. The process of producing alkali formaldehyde-sulfoxylate which comprises reducing an alkali-formaldehyde-bisulfite by means of spongy zinc electrolytically'pre pared.
5. The process of producing alkali formaldehyde-sillfoxylate which comprises reducing an alkali-formaldehyde hydrosulfite by means of spongy zinc electrolytically prepared. v
6. The process of producing sodium-formaldehyde sulfoxyl'ate which comprises re ducing sodium-formaldehyde-bisulfite by means of spongy zinc electrolytically prepared. I
7. The process of producing sodium-formaldehyde-sulfoxylate ducing sodium hydrosulfite-iormaldehyde by means of spongy zinc electrolytically pre pared.
In testimony whereof we have signed our names to this specification in the presence of two subscribing witnesses.
l-lEINRICH SPECKETER: EDUARD MARBUBG. Witnesses:
JEAN GRUND, ELSE Menus.
which comprises re-.
US81606314A 1914-02-02 1914-02-02 Manufacture of reduction products of sulfurous acids and salts thereof. Expired - Lifetime US1169365A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US81606314A US1169365A (en) 1914-02-02 1914-02-02 Manufacture of reduction products of sulfurous acids and salts thereof.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US81606314A US1169365A (en) 1914-02-02 1914-02-02 Manufacture of reduction products of sulfurous acids and salts thereof.

Publications (1)

Publication Number Publication Date
US1169365A true US1169365A (en) 1916-01-25

Family

ID=3237381

Family Applications (1)

Application Number Title Priority Date Filing Date
US81606314A Expired - Lifetime US1169365A (en) 1914-02-02 1914-02-02 Manufacture of reduction products of sulfurous acids and salts thereof.

Country Status (1)

Country Link
US (1) US1169365A (en)

Similar Documents

Publication Publication Date Title
US4514578A (en) Process for the preparation of trimethylolpropane
CN101486632A (en) Preparation of aluminum acetylacetonate
US2787628A (en) Reaction of carbon monoxide with hydrogen to form alcohols
US2654779A (en) Method of preparation of guanidino fatty acids
US1169365A (en) Manufacture of reduction products of sulfurous acids and salts thereof.
US4014939A (en) Process for producing formaldehyde
NO137891B (en) PROCEDURES FOR THE PREPARATION OF AROMATIC HYDROXYALDEHIDS
CN110078103A (en) A kind of calcium aluminium houghite and preparation method thereof
JPS6222740A (en) Isolation of p-hydroxybenzaldehyde
US2665313A (en) Production of 1, 6-naphthalenediol
US2357261A (en) Preparation of dicyandiamide salts
US3007853A (en) Process for purifying acrylonitrile
JPS5945666B2 (en) Method for producing aminocarboxylic acids
JP3048213B2 (en) Method for producing tris (acetylacetonato) ruthenium (III)
US2445500A (en) Manufacture of ethers of phenols
JPS61200935A (en) Production of p,p'-biphenol
US3968176A (en) Process for producing pentaerythritol
JPS62114943A (en) Method of purifying isophorone diamine
US3360534A (en) Method of producing a guanyl-o-alkylisourea salt
JPS6127980A (en) Preparation of hydroxyflavan compound
US3282648A (en) Process for the preparation of nickel carbonyl from nickel chloride and carbon monoxide
JPWO2005090275A1 (en) Hexahydroxytriphenylene monohydrate crystals and process for producing the same
JP4641640B2 (en) Method for producing carbodihydrazide
JP2000159716A (en) Production of orthoester
US2497063A (en) Process for the production of alkali metal phytates