US1984757A - Process of decomposing thiocyanic acid - Google Patents
Process of decomposing thiocyanic acid Download PDFInfo
- Publication number
- US1984757A US1984757A US537508A US53750831A US1984757A US 1984757 A US1984757 A US 1984757A US 537508 A US537508 A US 537508A US 53750831 A US53750831 A US 53750831A US 1984757 A US1984757 A US 1984757A
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- US
- United States
- Prior art keywords
- decomposing
- acid
- thiocyanic acid
- thiocyanic
- steel
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- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/24—Sulfates of ammonium
- C01C1/245—Preparation from compounds containing nitrogen and sulfur
Definitions
- the present invention relates to a process of decomposing thiocyanic acid, more particularly it relates to a process of decomposing thiocyanic acid and salts thereof by means of sulfuric acid in the presence of ammonium sulfate and in apparatus being constructed of or lined with chromium-nickel steel.
- thiocyanates are hydrolyzed by means of dilute acids, such as sulfuric acid, phosphoric acid or similar acids or also mixtures of these acids with the production of the.
- ammonium salt corresponding to the acid is effected by heating thiocyanates with these acids advantageously under pressure, totemperatures exceeding 100 C., for example, to 140,
- the attack on the metallic apparatus in the hydrolysis of the thiocyanic acid by means of sulfuric acid is considerably reduced, provided that the reaction is carried out in the presence of ammonium sulfate.
- steels which consist of 18-30% of Cr, 20-4% of Ni, 2-4% of Mo and 0.1-0.4% of C,
- ExampZa-A mixture of 3 parts by weight of ammonium thiocyanate, '4 parts by weight of concentrated sulfuric acid and parts by weight of an aqueous solution containing 35-40% of ammonium sulfate is heated for several hours to -180 C. in an autoclave consisting of chromium-nickel steel containing molybdenum. Complete hydrolysis of the ammonium thiocyanate then occurs with formation of ammonium sulfate and the apparatus is not substantially corroded.
- step 1 which comprises heating the thiocyanic acid in the presence of sulfuric acid and ammonium sulfate which has been added before the reaction to a temperature between about 100 and C. in an apparatus the corrodable parts whereof consist at least on the surface of chromium-nickel steel.
- step 2 which comprises heating the thiocyanic acid in the presence of sulfuric acid and ammonium sulfate which has been addedbefore the reaction to a temperature between 100 and 180 C. in an apparatus the corrodable parts whereof consist at least on the surface of chromium-nickel-molybdenum steel.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented Dec. 18, 1934 PATENT OFFICE PROCESS OF DECODgIPOSING THIOCYANIC A D Fritz Overdick, Leverkusen/Wiesdorf, Germany,
assignor to I. G. Farbenindustrie Aktiengesellschaft, Frankfort on the Main, Germany N0 Drawing. Application May "14, 1931, Serial No. 537,508. In Germany June 5, 1930 2 Claims. (01. 23-119 The present invention relates to a process of decomposing thiocyanic acid, more particularly it relates to a process of decomposing thiocyanic acid and salts thereof by means of sulfuric acid in the presence of ammonium sulfate and in apparatus being constructed of or lined with chromium-nickel steel.
It is known that thiocyanates are hydrolyzed by means of dilute acids, such as sulfuric acid, phosphoric acid or similar acids or also mixtures of these acids with the production of the.
ammonium salt corresponding to the acid. I This is effected by heating thiocyanates with these acids advantageously under pressure, totemperatures exceeding 100 C., for example, to 140,
to 180 c.
The reaction proceeds according to the following steps:
or summarized:
This process has however been found to be of the apparatus employed since almost all the metallic materials coming into question are strongly attacked by the hot acids or by the thiocyanic acid primarily produced. Even the chromium nickel steels which consist of 15-40% of Cr, 20- 1% of Ni and up to 1% of C; or 63-25% of Cr, 20 /3% of Ni and up to 1% of C; or 18-24% of Cr, 720% of Ni, 2-6% of Cu and 0.1-0.4% of C; or 18-30% of Cr, 20-4% of Ni, 24% of Mo and 0.1-0.4% of C, which otherwise are very resistant to acids have been found not to be durable in the process described. v
In accordance with the present invention the attack on the metallic apparatus in the hydrolysis of the thiocyanic acid by means of sulfuric acid is considerably reduced, provided that the reaction is carried out in the presence of ammonium sulfate.
Particularly resistant to corrosion are in this case steels, which consist of 18-30% of Cr, 20-4% of Ni, 2-4% of Mo and 0.1-0.4% of C,
as, for instance, a steel having the following composition:
Feresidue Obviously it is not necessary to construct the whole apparatus of this molybdenum steel, it is sufficient to line with this special steel those parts of the apparatus coming into contact with the reactionsolution. In the case of apparatus lined with acid resistant masonry only the fittings-(for example, heating and thermometertubes)-need be constructed 'of molybdenum steel. 1 I
The following example illustrates the invention without restricting it thereto:
ExampZa-A mixture of 3 parts by weight of ammonium thiocyanate, '4 parts by weight of concentrated sulfuric acid and parts by weight of an aqueous solution containing 35-40% of ammonium sulfate is heated for several hours to -180 C. in an autoclave consisting of chromium-nickel steel containing molybdenum. Complete hydrolysis of the ammonium thiocyanate then occurs with formation of ammonium sulfate and the apparatus is not substantially corroded.
I claim:-
1. In the process of decomposing thiocyanic acid by means of a mineral acid the step which comprises heating the thiocyanic acid in the presence of sulfuric acid and ammonium sulfate which has been added before the reaction to a temperature between about 100 and C. in an apparatus the corrodable parts whereof consist at least on the surface of chromium-nickel steel.
2. In the process of decomposing thiocyanic acid by means of a mineral acid the step which comprises heating the thiocyanic acid in the presence of sulfuric acid and ammonium sulfate which has been addedbefore the reaction to a temperature between 100 and 180 C. in an apparatus the corrodable parts whereof consist at least on the surface of chromium-nickel-molybdenum steel.
- FRITZ OVERDICK.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1984757X | 1930-06-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
US1984757A true US1984757A (en) | 1934-12-18 |
Family
ID=7884578
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US537508A Expired - Lifetime US1984757A (en) | 1930-06-05 | 1931-05-14 | Process of decomposing thiocyanic acid |
Country Status (1)
Country | Link |
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US (1) | US1984757A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2712980A (en) * | 1952-09-06 | 1955-07-12 | Richard D Hoak | Process for using sulphate liquors for recovering values from coke oven gas |
-
1931
- 1931-05-14 US US537508A patent/US1984757A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2712980A (en) * | 1952-09-06 | 1955-07-12 | Richard D Hoak | Process for using sulphate liquors for recovering values from coke oven gas |
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