PROCESS FOR PRODUCING CYANURIC ACID

Abstract: A men of preparing cyanuric acid wherein molten urea is heeted up to the temperature rnnge of from 180° C to a 300° C by the use of high-frequency dielectric heating. The molten urea may be either molten urea substantially com­ posed of uraa or molten urea which includes molten biurets. The molten urea is converted to cyanuric acid by the genera­ tion of heat caused by the dielectric loss in a high-frequency electric field. It will be noted that cyanuric acid does not gen­ erate heat. Thus, this invention eliminates the disadvantages of the conventional methods, such as poor heat transfer to the reaction system, contamination of product by raw mater­ ial, excess heating of product adhesion of product to the walls of reaction vessel and the like.

Description: DESCRIPTION Technical Field: This invention relates to a process of producing cyanuric acid from urea. Background Art: The commercial processes of producing cyanuric acid (hereinafter referred to as "CA") using urea as the starting raw material consist basically of heating urea at 180 X 3000C for several hours to convert it to CA with evolution of ammonia gas. However, the conversion of urea to CA in the commercial operation involves such difficulties as summarized below; (a) The reaction mass solidifies in the course of conversion, and it turns to an inclusion containing urea, biuret, CA and others which requires additional heating to con vert the remained urea and biuret to CA, however, the additional heating is not carried out effectively because of poor heat conduction of the solidified reaction mass. (b) an excessive heating of the solidified reaction mass necessary for converting the intermediates into CA causes decomposition of CA formed in the mass. (c) the solidified reaction product adheres so str.ongly to the wall of the reactor that the removal of produt from the reactor is difficult. Numerous methods have been proposed to overcome these problems, and they include such troublesome processes as employing a pulverized mixture of urea and the recycled CA for the starting raw material to be heated, as shown for example in the Japanese published examined patent applidation No. 49-25676 (1974). It is therefore an object of this invention to provide a process of producing CA from urea, whereby it is possible to overcome difficulties existed in the convertional processes. It is another object of this invention to provide a process of the type described, whereby the process is suitable for the commercial'prduction of CA from urea. Disclosure of Invention: In a process of producing cyanuric acid by heating urea at 180 X 300"C, the present invention consists of heating a fused state urea by means of a high frequency induction heating method. Best Mode of Carrying Out the Invention: The fused state urea used as the starting raw material of this invention is prepared by heating conventionally available solid urea at a temperature above its melting point of about 1350C. The fused state urea is not necessarily composed of substantially pure melted urea but it may contain an amount of melted biuret which is formed when urea is heated to obtain melted urea. Accordingly, the fused state urea is preferably prepared by heating urea at about 140 X 1500C for obtaining the substantially pure melted urea, or by hearing urea at about 160 X 2000C for obtaining a melted state urea containing up to about 30% of biuret. When the fused state urea is placed in a high frequency electric field, it is susceptible of generating heat due to its dielectric loss, and the dielectric heat thus generated converts the urea or biuret to CA. Since the generation of dielectric heat occures internally in molecules of melted urea or melted biuret, the heating method eliminates the heat transfer problem of the conventional methods employing the external heating of the reaction mass. Furthermore, the generation of dielectic heat occures solely in melted urea and melted biuret,'and does not occure in the product CA. That is to say, the heat generation continues so far as the raw material remains in the reaction mass, and after the entire raw material has been converted to solid CA, the heat gereration ceases. Accordingly, the inclusion of the raw material in the solid CA, and the excessive heating of the product are minimized. Since the chemical reaction according to this invention is same with that of the conventional process, the temperature applied for heating of the reaction mass in this invention may be 180 X 3000C. However, due to the efficient heating system of this invention, the duration of heating is reduced remarkably to 3 X 30 minutes, although it depends on the temperature of reaction mass. The preferable heating conditions are composed of maintaing the reaction mass at 200 X 2500C for the duration of 5 X 20 minutes. Under these condifions, the reaction mass can be heated in vessels made of such electrically non conductive materials as heat-resistant glass and heat-resistant plastics like glassfiber reinforced fluorocarbon resin, so that the product CA can be removed quite easily from the rection vessel. Apparatus employed for the high frequency induction heating are usually composed of electrodes and high frequency generators, and such factors as the shape, dimension and arrangement of the electrodes as well as the frequency and electrical power of the generators can be selected properly in accordance with the process conditions. The preferable frequeneies of the generator are 10 X 3000MHz, and the prefer- able shape of the electrode is parallel metal sheets. When the fused state urea is set in the high frequency induction heating apparatus, and electrical power is supplied to maintain the reaction mass at the desired temperature, the reaction proceeds with evolution of ammonia gas. The power consumption for the heating continues until the reaction mass is converted entirely to solid CA, so that proceeding of the reaction may favorablly be checked by the power consum,?tior.. The product CA thus obtained usally contain about 20 t 30% of impurities comprising mostly ammelide and ammeline. -herefore, the crude CA is treated with a 10% sulfuric acid to ctain purified CA. industrial Applicability: According to the present invention, CA can be prz¯lced easily from urea in the yield of above 80%, so that tYe process is suitable for the commercial operation of Q produc ton. Example 1. Solid urea was heated at about 1500C to prepare substantially pure melted urea. Into a 200 mZ heat-resistant glass beaker was charged 100g of the melted urea, and the beaker was inserted between parallel metal sheets electrodes connected with a high frequency gererator for 27.12MHz. By supplying electrical power to the generator, the content in the beaker began to be heated, and turned gradually to opaque with evolution of ammonia gas. Under controlling the power supply, the reaction mass was maintained at 200 X 2500C for about 10 minutes. The solid white product of 60.4g thus obtained hac the composition of CA 76.4%, ammelide 20.7% and others 2.9%. The crude CA was treated with a 10% sulfuric acid to obtain 58.2g CA. The yield was 81.1%. Example 2. One hundred gram of substantially pure melted urea in a 200 mQ heat-resistant glass beaker was heated with a high frequency induction heater for 2450MHz. After heating the content at 200 X 2500C for 8 minutes, 62.0g of white solid was obtained. The crude CA had the composition of CA 78.3%, ammelide 20.4% and others 1.3%. By treating it with a 10% sulfuric acid was obtained 60.lg of CA in 83.9% yield. Example 3. Into a glassfiber reinforced fluorocarbon resin pan was charged 675g of a fused state urea which contained about 7% of biuret formed during heating of urea at 1700C. The fused state urea in the pan was placed on parallel elcetrodes composing a grid electrode type high frequency induction heater for 13.56MHz. After heating the content at 200 X 2500C for 15 minutes, 430g of white solid was obtained. The crude CA had the composition of CA 66.6%, ammelide 31.8% and 1.6% others. The yield of purified CA was 79%.

Claims: CLAIMS 1. In a process of producing cyanuric acid comprising the step of heating urea at from 1800C to 3000C, the improvement wherein said heating of urea is carried out by heating a fused state urea by means of a high frequency induction heating method. 2. A process as claimed in Claim 1, wherein said fused state urea is substantially pure melted urea or a melted state urea containing melted biuret. 3. A process as claimed in Claim 2, wherein said melted state urea contains melted biuret of up to 30%. 4. A process as claimed in Claim 1, wherein said heating is carried out at from 2000C to 2500C. 5. A process as claimed in Claim 1, wherein said high frequency induction heating employs high frequency eletric current of from 10MHz to 3000MHz.

Inventors: ICHIHARA, RYOICHI, KIKUCHI, ICHIRO 2510-1, SIMONAGAYA-CHO KOONAN-KU, KIZAWA, HIDENORI, YAO, TOSHIO
Applicants: NIPPON SODA CO., LTD.
Application year: 1979
Main classification: C07D251
IPC codes: C07D251