US2957751A - Method of producing cyanogen from cuprous cyanide - Google Patents
Method of producing cyanogen from cuprous cyanide Download PDFInfo
- Publication number
- US2957751A US2957751A US770312A US77031258A US2957751A US 2957751 A US2957751 A US 2957751A US 770312 A US770312 A US 770312A US 77031258 A US77031258 A US 77031258A US 2957751 A US2957751 A US 2957751A
- Authority
- US
- United States
- Prior art keywords
- cyanogen
- cuprous cyanide
- tube
- cyanide
- temperature
- 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
- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 title claims description 45
- 238000000034 method Methods 0.000 title claims description 7
- DOBRDRYODQBAMW-UHFFFAOYSA-N copper(i) cyanide Chemical compound [Cu+].N#[C-] DOBRDRYODQBAMW-UHFFFAOYSA-N 0.000 title description 11
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- RBHJBMIOOPYDBQ-UHFFFAOYSA-N carbon dioxide;propan-2-one Chemical compound O=C=O.CC(C)=O RBHJBMIOOPYDBQ-UHFFFAOYSA-N 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052754 neon Inorganic materials 0.000 description 1
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229910001961 silver nitrate Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C3/00—Cyanogen; Compounds thereof
- C01C3/003—Cyanogen
Definitions
- the present invention relates to the preparation of cyanogen.
- Another object is to reduce the formation of paracyanogen in preparing cyanogen.
- a further object is to prepare cyanogen from cuprous cyanide.
- Yet another object is to avoid the formation of hydrolysis products in the preparation of cyanogen.
- cuprous cyanide in an inert atmosphere, preferably at atmospheric pressure at a temperature of at least 500 C. and preferably 800-850 C. Higher temperatures can be employed, e.g., as high as 1050 C. At temperatures above 860 C. no paracyanogen can form.
- nitrogen gas is the preferred inert atmosphere
- other inert gases such as helium, argon and neon. Yields of cyanogen of 95 to 100% of theoretical are obtained.
- the inert gas should be dry since water vapor partially hydrolyzes cuprous cyanide to CuOH and HCN.
- EXAMPLE 1 Into the porcelain combustion boat was weighed 2.7987 grams of cuprous cyanide. The boat was placed in the center of the combustion tube which in turn was heated by the furnace. A slow stream of dry nitrogen was passed through the tube and the bed gradually heated to 820 C. The reaction was held at this temperature for 3 hours and the gases swept out of the tube and collected in the gas scrubber containing 200 ml. of 1% sodium hydroxide as previously indicated. Cyanogen was obtained in an amount of 0.797 g. which was 98.8% of theory. 2.0 g. of metallic copper was recovered from the combustion boat.
- a process of preparing cyanogen comprising heating cuprous cyanide in an inert atmosphere at a temperature of at least 800 C.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
NIETHOD OF PRODUCING CYANOGEN FROM 'CUPROUS CYANIDE Frank J. Vancheri and Johnstone S. Mackay, Pittsburgh,
Pa., assignors to Pittsburgh Coke & Chemical Company, Pittsburgh, Pa., a corporation of Pennsylvania No Drawing. Filed Oct. 29, 1958, Ser. No. 770,312
5 Claims. (Cl. 23-151) The present invention relates to the preparation of cyanogen.
It has previously been proposed to prepare cyanogen at relatively low temperatures by the reduction of cupric cyanide to cuprous cyanide and cyanogen. It has also been proposed to heat cupric compounds in the presence of the cyanide ion in aqueous solutions to yield cyanogen. Unfortunately, at the temperatures required for such re actions, the cyanogen:paracyanogen equilibrium favors the polymer. Furthermore, water and acidic gases catalyze the decomposition of cyanogen to paracyanogen.
It is an object of the present invention to prepare cyanogen in increased yields.
Another object is to reduce the formation of paracyanogen in preparing cyanogen.
A further object is to prepare cyanogen from cuprous cyanide.
Yet another object is to avoid the formation of hydrolysis products in the preparation of cyanogen.
Still further objects and the entire scope of applicability of the present invention will become apparent from the detailed description given hereinafter; it should be understood, however, that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
It has now been found that these objects can be attained by heating cuprous cyanide in an inert atmosphere, preferably at atmospheric pressure at a temperature of at least 500 C. and preferably 800-850 C. Higher temperatures can be employed, e.g., as high as 1050 C. At temperatures above 860 C. no paracyanogen can form.
While nitrogen gas is the preferred inert atmosphere, there can also be employed other inert gases such as helium, argon and neon. Yields of cyanogen of 95 to 100% of theoretical are obtained. The inert gas should be dry since water vapor partially hydrolyzes cuprous cyanide to CuOH and HCN.
Unless otherwise stated, all parts and percentages are by weight.
In the following examples 2.5 to 3.0 g. samples were placed in a porcelain combustion boat which was then placed in the center of a one inch diameter Vycor combustion tube, and the tube placed in an electrical combustion furnace. A plug of glass wool was placed at the exit of the tube. The tube and contents were weighed on a trip scale. At the entrance of the tube was a rubber stopper with a glass tube exit which was connected with rubber tubing to a gas scrubber containing 200 ml. of 1% sodium hydroxide solution.
-A slow stream of nitrogen, 70-100 cc./ntin., was passed through the tube and the bed was gradually heated to the desired temperature, e.g., 820 C., using a 45 to 60 minute heat-up time. The temperature was recorded with a thermocouple and a potentiometer. 'Ihe cuprous 2,957,751 Patented a. 25, 1950 a cyanide was held on temperature for 0.5 to 3.0 hours. To prevent air from getting into the tube and oxidizing the copper residue, thenitrogen stream was left on during cooling.
5 The tube was weighed and the weight loss recorded. The residue in the boat was metallic copper. The caustic solution was diluted to 250 ml. and a 50 ml. aliquot was titrated for cyanide with 0.1 N silver nitrate. Cyanogen, based on the hydrolysis reaction:
( CN) +H O- HCN-l-HCNO was calculated and the molar yield reported. Also, CuCN was decomposed and the gases were condensed in a Dry Ice-acetone trap. The M.P. of the condensed liquid was 26 to -34 C. The reported M.P. of cyanogen is -34.4 C.
EXAMPLE 1 Into the porcelain combustion boat was weighed 2.7987 grams of cuprous cyanide. The boat was placed in the center of the combustion tube which in turn was heated by the furnace. A slow stream of dry nitrogen was passed through the tube and the bed gradually heated to 820 C. The reaction was held at this temperature for 3 hours and the gases swept out of the tube and collected in the gas scrubber containing 200 ml. of 1% sodium hydroxide as previously indicated. Cyanogen was obtained in an amount of 0.797 g. which was 98.8% of theory. 2.0 g. of metallic copper was recovered from the combustion boat.
The effect of temperature on the yields can be seen from the following table in which the reaction conditions were identical with those of Example 1 except for the indicated changes.
Table 1 Temper- CuCN (ON 3 Yield Example ature (g.) (g.) 11%]??? .0
1 A trace of Water in the nitrogen gas in this run resulted in a slightly higher than theoretical reported yield.
From this table, it can be seen that using a reaction time of 3 hours at 820 0., there was obtained a yield of over 98% cyanogen, while as the temperature was lowered the yield was reduced.
The effect of time of reaction is shown in Table 2 where all reactions were carried out at 820 C.
Table 2 Time CuCN (ON), Yield Example (hr.) (g.) (g.) Percent What is claimed is: l. A process of preparing cyanogen comprising heat- 7 ing cuprous cyanide in an inert atmosphere at a temperature of at least 500 C.
2. A process of preparing cyanogen comprising heating cuprous cyanide in an inert atmosphere at a temperature of at least 800 C.
3. A process according to claim 2 wherein the inert atmosphere is nitrogen gas.
4. A process according to claim 2 wherein the tem- 5 perature is 800 to 850 C.
5. A process according to claim 4 wherein the inert atmosphere is nitrogen gas and the reaction is carried out at atmospheric pressure.
References Cited in the file of this patent Williams: The Chemistry of Cyanogen Compounds and Their Manufacture and Estimation, publ. by J. and A. Churchill, London, 1915, page 3.
Claims (1)
1. A PROCESS OF PREPARING CYANOGEN COMPRISING HEATING CUPROUD CYANIDE IN AN INERT ATMOSPHERE AT A TEMPERATURE OF AT LEAST 500*C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US770312A US2957751A (en) | 1958-10-29 | 1958-10-29 | Method of producing cyanogen from cuprous cyanide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US770312A US2957751A (en) | 1958-10-29 | 1958-10-29 | Method of producing cyanogen from cuprous cyanide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2957751A true US2957751A (en) | 1960-10-25 |
Family
ID=25088124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US770312A Expired - Lifetime US2957751A (en) | 1958-10-29 | 1958-10-29 | Method of producing cyanogen from cuprous cyanide |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2957751A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3166390A (en) * | 1960-04-04 | 1965-01-19 | Carbogen Corp | Method of making hcno |
-
1958
- 1958-10-29 US US770312A patent/US2957751A/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3166390A (en) * | 1960-04-04 | 1965-01-19 | Carbogen Corp | Method of making hcno |
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