TWI237016B - Method and apparatus for preparing hydrazodicarbonamide using urea as starting material - Google Patents

Method and apparatus for preparing hydrazodicarbonamide using urea as starting material Download PDF

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TWI237016B
TWI237016B TW091100904A TW91100904A TWI237016B TW I237016 B TWI237016 B TW I237016B TW 091100904 A TW091100904 A TW 091100904A TW 91100904 A TW91100904 A TW 91100904A TW I237016 B TWI237016 B TW I237016B
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Taiwan
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ammonia
reaction
biuret
azidomethoxamine
preparing
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TW091100904A
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Chinese (zh)
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Chun-Hyuk Lee
Sang-Jin Han
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J & J Chemical Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C231/00Preparation of carboxylic acid amides
    • C07C231/14Preparation of carboxylic acid amides by formation of carboxamide groups together with reactions not involving the carboxamide groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C231/00Preparation of carboxylic acid amides
    • C07C231/02Preparation of carboxylic acid amides from carboxylic acids or from esters, anhydrides, or halides thereof by reaction with ammonia or amines

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  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention relates to a method and apparatus for preparing hydrazodicarbonamide using urea as starting material economically and environmentally desirably. The apparatus includes a pyrolysis furnace to obtain biuret and ammonia by pyrolyzing urea; a recrystallization reactor to purify the biuret obtained from the pyrolysis furnace; a first reactor to obtain an metal monohalobiuret salt by reacting the biuret with metal hypohalogen compound or with halogen and base; a second reactor to synthesize the hydrazodicarbonamide by reacting the monohalobiuret metal salt with ammonia; and an ammonia evaporator to separate the excess ammonia from hydrazodicarbonamide and to supply the separated ammonia to an ammonia concentrator.

Description

1237016 A7 B7 五、發明説明() 發明領域: 本發明係關於一種以尿素為起始物來製備疊氮甲醯胺 的方法及其設備。具體而言,本發明係關於一種以尿素 來生成縮二將’並以所生成(縮二脾與於合成縮二膦期間 所生成的銨互相反應,來經濟、環保地製備疊氮甲醯胺 的方法及其設備。 發明背景: 疊氮 T 醯胺(hydrazodicarbonamide,HDCA)為製備偶 氮甲酿胺的一種非常有用的起始物,至於偶氮甲酿胺則 是一種被廣泛使用的泡床劑。如反應式1所示,偶氮甲 醯胺(2)可藉由適當氧化劑氧化疊氮甲醯胺(1)而得。 [反應式1] ........................訂 (請先閲讀背面之注意事項再填寫本頁) [〇1 〇 ΟII II h2n-c-nh-nh-c-nk ⑴ h2n-c-n=n-c-nh2(2) 經濟部智慧財產局員工消費合作社印製 傳統製備疊氮甲醯胺的方法包括(i)以聯胺為起始物’ (ii)以尿素進行直接合成,(iii)以尿素來製備氨基脲’接 著將所製得的氨基脲轉變成疊氮甲醯胺,及(iv)以縮二脾 為起始物。 在以聯胺為起始物的製備方法中(反應式2)’疊氣甲 醯胺係藉由讓1莫耳的聯胺(3)與2莫耳的尿素(4)反應所 製得, 第頂 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公楚) 1237016 A 7 B7 經濟部智慧財產局員工消費合作社印製 五、發明説明() [反應式2] 0 0 0 H2NNH2 4. H2N-C-NH2--- H2N-C-NH-NH-C-NH2 + 2 nh3 (3) (4) ^ 上述反應式的優點在於其製程簡單,但其缺點則在於 其所使用的起始物-聯胺,價格昂貴且不易合成。可製備 聯胺的代表性方法包括拉辛法(Rasehing process)及使用 酮連氮(ketazine)的方法。但是,由這些方法所獲得的聯 胺還需經濃縮及水解處理方能使用。因此,造成製程所 需消耗的能源太高’造成生產成本上升。另外,聯胺亦 可藉由讓尿素與次氯酸鋼及氫氧化訥反應的尿素法來進 ^亍製備。但此方法需要使用過量的氫氧化鈉,且其用來 移除碳酸鈉副產物的成本太鬲,並需使用許多化學物方 能移除其反應副產物。因此,此方法被認為不符環保及 經濟效益。 下列反應式3代表以尿素直接合成疊氮甲醯胺的方 法。如反應式3所示,3莫耳尿素與4莫耳氫氧化鈉及i 莫耳氯氣反應可得1莫耳的疊氮甲醯胺。但是,此方法 亦有其缺點’因為其需使用過量試劑且製程複雜,故造 成成本太高。另一問題是會產生許多對環境不利的氨副 產物。 (請先閲讀背面之注意事項再填寫本頁) 裝- 再填寫本一 · f 第頂本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 A7 B7 五、發明説明( [反應式3 ;) ?\ H2N-C-NH2 +4Na〇H+a ο 9 II 丨丨 H N-C-NH-NH-C-NH. + 2 NaCl + 2 H2 Ο + 叫03 + 2 NH〕 下列反應式4顯示另一合成疊氮甲醯胺的方法。本方 法包含以尿素製備氨基脲的步驟,及接著將所得氨基脲轉 變成疊氮甲醯胺的步驟。如反應式4所示,尿素與次氯 酸納反應可得單氯化尿素鈉鹽,該單氯化尿素鈉鹽在催 化劑存在下與過量氨反應可得中間物-氨基脲,之後讓所 知〈氨基脾與尿素反應,可得終產物-疊氮甲醯胺。 [反應式4] 請 先 閲 讀 背 面 之 注 意 事 項 再 填 寫 本 頁 H2N-C-NH2 4- NaOC! H2N-C-NH-NH« NaCI -f· H2 〇1237016 A7 B7 V. Description of the invention () Field of the invention: The present invention relates to a method and equipment for preparing azidomethoxamine using urea as a starting material. Specifically, the present invention relates to a method for generating bipyridine with urea and reacting the generated (biple spleen and ammonium generated during the synthesis of biphosphine) with each other to economically and environmentally produce azidomethamine. BACKGROUND OF THE INVENTION: Azido Tamine (hydrazodicarbonamide, HDCA) is a very useful starting material for the preparation of azomethamine, and azomethamine is a widely used bubble bed As shown in Reaction Formula 1, azomethoxamine (2) can be obtained by oxidizing azidomethoxamine (1) with an appropriate oxidant. [Action formula 1] ........... ............. Order (Please read the notes on the back before filling this page) [〇1 〇〇II II h2n-c-nh-nh-c-nk ⑴ h2n-cn = nc -nh2 (2) The traditional method for preparing azidomethoxamine by the consumer cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs includes (i) starting with hydrazine '(ii) direct synthesis with urea, (iii) urea To prepare a semicarbazide ', and then convert the prepared semicarbazide to azidemethoxamine, and (iv) bisplendium as the starting material. In the preparation method using hydrazine as the starting material ( Application formula 2) 'Azomethanamine is prepared by reacting 1 mole of hydrazine (3) and 2 mole of urea (4). The first paper size applies Chinese National Standard (CNS) A4 Specifications (210X297) Chu 1237016 A 7 B7 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention () [Reaction formula 2] 0 0 0 H2NNH2 4. H2N-C-NH2 --- H2N-C-NH -NH-C-NH2 + 2 nh3 (3) (4) ^ The advantage of the above reaction formula is that the process is simple, but the disadvantage is that the starting material used is hydrazine, which is expensive and difficult to synthesize. Can be prepared Typical methods of hydrazine include the Rasehing process and the method using ketazine. However, the hydrazine obtained by these methods also needs to be concentrated and hydrolyzed before it can be used. Therefore, the manufacturing process is caused The energy consumption required is too high, which results in increased production costs. In addition, hydrazine can also be prepared by the urea method that reacts urea with steel hypochlorite and sodium hydroxide. However, this method requires the use of excess hydrogen Sodium oxide, which is too expensive to remove by-products of sodium carbonate, and requires many chemicals The reaction by-products can only be removed. Therefore, this method is considered to be incompatible with environmental protection and economic benefits. The following reaction formula 3 represents a method for directly synthesizing azidomethoxamine from urea. As shown in reaction formula 3, 3 moles of urea and The reaction of 4 mole sodium hydroxide and 1 mole chlorine can obtain 1 mole of azidomethanamine. However, this method also has its disadvantages' because it requires the use of excess reagents and the manufacturing process is complicated, so the cost is too high. Another One problem is that many byproducts of ammonia that are not environmentally friendly are produced. (Please read the precautions on the back before filling this page) Packing-then fill in this one. F The top paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 1237016 A7 B7 V. Description of the invention ([Reaction Formula 3;)? H2N-C-NH2 + 4Na〇H + a ο 9 II 丨 丨 H NC-NH-NH-C-NH. + 2 NaCl + 2 H2 〇 + called 03 + 2 NH] The following reaction formula 4 shows another method for synthesizing azidomethoxamine. The present method includes a step of preparing semicarbazide from urea, and then a step of converting the obtained semicarbazide to azidomethoxamine. As shown in reaction formula 4, the reaction between urea and sodium hypochlorite can obtain the sodium monochloride urea, and the sodium monochloride urea reacts with excess ammonia in the presence of a catalyst to obtain the intermediate-semicarbazide, which will be known later <The amino spleen reacts with urea to obtain the final product, azidomethoxamine. [Reaction formula 4] Please read the notes on the back first and then fill in this page. H2N-C-NH2 4- NaOC! H2N-C-NH-NH «NaCI -f · H2 〇

Ο II H^N-C-NH-NH ο II h2n-c-nh2 o o u 丨 I II H2N-0-NH-NH-C-NHo + NHn 經濟部智慧財產局員工消費合作社印製 基 5氨 達得 高 可 用方 使劑 需化 鹽催 鋼的 素貴 尿昂 化用 氣使 單需 位是 單或 每, 因 亦 應 反 此 但 氨 量 過 的 上 以 倍 o o 變 案 轉 青 膊 .言 基 申 氨 際 將 需 目長Mi 是很 題得二 問變縮 個間以 一 時 卜程示 夕 考 另製顯 。 使 5 益 , 效故式 、濟k應 經胺 符醯反 不甲列 而 氮 , 田« 脲成 下 頁 勒 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公复) 1237016 A7 B7 五、發明説明() PCT7KR8 8/0 1 8 0)合成疊氮甲醯胺的方法。其包含讓縮二 脲與次鹵化金屬(MOX)反應以生成單鹵化縮二脲金屬鹽的 步驟,及後續將所得之單齒化縮二脲金屬鹽與氨反應來 製備疊氮甲si胺的步驟。 [反應式5] 0 0 0 0 〇 9 II \\ II ί! II 11 H2N-C-NH-C-NH2 -f ΜΟΧ —H2N-C-N-C-NH or H2N-C-N-C-NH + h2 0〇 II H ^ NC-NH-NH ο II h2n-c-nh2 oou 丨 I II H2N-0-NH-NH-C-NHo + NHn Intellectual Property Bureau, Ministry of Economic Affairs, Employee Consumer Cooperative Printed Base 5 The prescription requires the salt to urge the steel to make the expensive urine, and the gas is used to make the unit demand is single or per unit. Therefore, it should also be reversed, but the amount of ammonia is increased by oo. The change is blue. The length of the head Mi is very different, and the second question will be shortened, and the test will be displayed separately. To make 5 benefits, the formula is to use the amine symbol instead of nitrogen. Tian «Urea is the next page. The size of this paper applies the Chinese National Standard (CNS) A4 specification (210X 297 public copy) 1237016 A7 B7 V. Description of the invention () PCT7KR8 8/0 1 8 0) Method for synthesizing azidomethoxamine. It comprises the steps of reacting biuret with a metal hypohalide (MOX) to form a monohalide biuret metal salt, and subsequently reacting the obtained monodentate biuret metal salt with ammonia to prepare azidomethyl siamine. step. [Reaction formula 5] 0 0 0 0 〇 9 II \\ II ί! II 11 H2N-C-NH-C-NH2 -f ΜΟχ —H2N-C-N-C-NH or H2N-C-N-C-NH + h2 0

XX

0 0 H2N.C-N-C-NH or η,ν-c-n-c-nh + nh3 I I I i X M MX ? h2n-c-nh-nh-c-nh2 經濟部智慧財產局員工消費合作社印製 但是’上述以縮二脲為起始物來製備疊氮甲醯胺的方 法亦有缺點,在於作為起始物的縮二解價格昂貴或含許 多雜質,且以縮二脲與氨反應來製備燊氮甲醯胺的反應 需使用許多額外的氨,故本法亦不符環保及經濟效益。 發明搞沭 本發明目的之一係提供一種以價格便宜且易於取得之 尿素作為起始物來經濟、環保地製備疊氮甲醯胺的方法。 本發明之另一目的係提供一種可使用最少起始物及產 生最少副產物之製備疊氮甲醯胺的方法及設備。 本發明之另一目的係提供一種藉由連續執行製程以獲 得高產率之製備疊氮甲醯胺的方法及設備。 為達上述這些目的,本發明提供一種製備疊氮甲醯胺 第5頁0 0 H2N.CNC-NH or η, ν-cnc-nh + nh3 III i XM MX? H2n-c-nh-nh-c-nh2 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, but 'the above is biuret The method for preparing azidomethoxamine as a starting material also has disadvantages in that the bispyrolysis as a starting material is expensive or contains many impurities, and the reaction of preparing biazidine with biuret and ammonia A lot of extra ammonia is needed, so this law is not environmentally friendly and economical. Disclosure of the Invention One of the objects of the present invention is to provide a method for economically and environmentally-friendly preparation of azidomethoxamine using urea, which is cheap and easily available, as a starting material. Another object of the present invention is to provide a method and apparatus for preparing azidomethoxamine which can use the least starting materials and produce the least by-products. Another object of the present invention is to provide a method and apparatus for preparing azidomethoxamine by continuously performing a process to obtain a high yield. In order to achieve the above-mentioned objects, the present invention provides a method for preparing azidomethoxamine. Page 5

1237016 A7 B7 五、發明説明() 的方法,其係包含熱解尿素來製備式1之縮二脲及氨的 步驟;讓所製備而得的縮二脲與次卣化金屬化合物(或與 鹵素與驗)反應,以獲得式2或式3之單卣化縮二脾金屬 鹽的步驟;及讓所得之單函化縮二脲金屬鹽與氨反應的 步驟。 [式1] 〇 〇1237016 A7 B7 5. The method of the invention description (), which comprises the steps of pyrolyzing urea to prepare biuret and ammonia of formula 1; letting the biuret and the hypohalide metal compound (or halogen And a step of reacting) to obtain a mono-bilated bisplen metal salt of Formula 2 or Formula 3; and a step of reacting the obtained mono-functional biuret metal salt with ammonia. [Formula 1] 〇 〇

II II h2n^c-nh-c-nh2 [式2]II II h2n ^ c-nh-c-nh2 [Formula 2]

HaN-〇-N-〇-fs4H X Μ [式3]HaN-〇-N-〇-fs4H X Μ [Formula 3]

H2N-0-N-C-NH 在上述式2及式3中,Μ代表金屬且X代表i素。尿 素的熱解溫度較佳係介於100°C至300°C間,且該熱解過 程較佳係在移除氨時執行,且讓所移除的氨與單齒化縮 二脲金屬鹽反應。 本發明更提供一種製備疊氮甲醯胺的設備,其係包含 第6頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 、τ f 經濟部智慧財產局員工消費合作社印製 1237016 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明説明( 一可熱解尿素以得縮二脲及氨的熱解爐;一可讓所獲得 之縮二脲與次1¾化金屬化合物(或!I素與鹼)反應,以得單 鹵化縮二脲金屬鹽之第一反應器;一可讓所得之單鹵化 縮二脲金屬鹽與氨反應以合成疊氮甲醯胺的第二反應 器;及一可將過量氨與疊氮甲醯胺分開,並將所分離出 的氨導向氨濃縮器之氨揮發器。 該氨濃縮器較佳係可濃縮過量的氨及於熱解爐中所生 成的氨,並將所濃縮的氨提供給第二反應器使用。該熱 解爐可包含一可注入惰性氣體的氣體注入口,該惰性氣 體係不會與進入熱解爐中的異氰酸反應,且該熱解爐還 可包含一種可降低壓力以便能自熱解爐中移除氨的手 段。 附圖簡述 藉由以下附圖將可更瞭解本發明及其優點,其中: 第1圖係顯示依據本發明一實施例來製備疊氮甲醯胺 之設備的流程圖。 圖號對照說明 10 12 20 30 32、54 熱解爐 氣體注入口 氨濃縮器 再結晶器 脫水器 第頂 本紙張尺度適用中國國家標準(CNS)A4規格(210Χ 297公釐) 1237016 A 7 B7 五、發明説明() 40 第一反應器 50 第二反應器 (請先閲讀背面之注意事項再填寫本頁) 52 氨揮發器 發明詳細說明 下面詳細說明只列出本發明之較佳實施例,藉以說明 實施本發明之最佳模式。需知,本發明尚可做許多改良 及變化,這些改良及變化都應仍視為本發明之範疇,故 本發明之附圖及詳細說明,僅係為闡述本發明,本發明 之範疇並不僅限於此。 依據本發明製備疊氮甲醯胺,首先,在高於尿素融點 之溫度熱解尿素,以生成式1之縮二脲及氨。一般而言, 縮二脲被廣泛用作為藥物、殺草劑、及分析試劑的前驅 物,同時亦被大量作為囉齒動物之飼料,並被廣泛應用 於各塑膠樹脂領域中。此外,已知某些縮二脲衍生物亦 具有生理癒合劑或化療藥劑的功能。下列反應式 6顯示 以熱解尿素來合成縮二脲的製程。 [反應式6] 經濟部智慧財產局員工消費合作社印製 9 9 〇〇 II il heat II || H2N-C-NH2 + H2N-C-NH2 -- h2n-c-nh-c-nh2 + nh3 如反應式6所示,熱解2莫耳尿素,並移除氨,可產 第8頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 A7 B7 五、發明説明( 生縮二脲。具體而言,如下列反應式7所示,一般假設 首先在熱解尿素時’會產生異氰酸及氨,之後才會產生 標的產物-縮二脲。 [反應式7] heat H-N=C-0 + NH, 請 先 閲 讀 背 面 之 意 事 項H2N-0-N-C-NH In the above formulae 2 and 3, M represents a metal and X represents an i prime. The pyrolysis temperature of urea is preferably between 100 ° C and 300 ° C, and the pyrolysis process is preferably performed when ammonia is removed, and the removed ammonia and the monodentate biuret metal salt reaction. The present invention further provides a device for preparing azidomethoxamine, which includes the paper size on page 6 which is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) (Please read the precautions on the back before filling this page) , Τ f Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 1237016 A7 B7 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of the invention (a pyrolysis furnace that can pyrolyze urea to obtain biuret and ammonia; The first reactor in which the obtained biuret is reacted with a secondary metal compound (or! I and a base) to obtain a monohalogenated biuret metal salt; a monorehalable biuret metal salt can be obtained A second reactor that reacts with ammonia to synthesize azidomethoxamine; and an ammonia volatilizer that separates excess ammonia from azidomethoxamine and directs the separated ammonia to an ammonia concentrator. Preferably, the excess ammonia and the ammonia generated in the pyrolysis furnace can be concentrated, and the concentrated ammonia can be provided to the second reactor for use. The pyrolysis furnace may include a gas injection port capable of injecting an inert gas, the Inert gas system will not The isocyanate reaction in the furnace, and the pyrolysis furnace can also include a means to reduce the pressure so that ammonia can be removed from the pyrolysis furnace. BRIEF DESCRIPTION OF THE DRAWINGS The invention and its understanding will be better understood from the following drawings. Advantages, of which: Fig. 1 is a flow chart showing a device for preparing azidomethoxamine according to an embodiment of the present invention. Drawing No. Comparative Description 10 12 20 30 32, 54 Reconcentration of ammonia concentrator in gas injection port of pyrolysis furnace The paper size of the dehydrator is applicable to the Chinese national standard (CNS) A4 specification (210 × 297 mm) 1237016 A 7 B7 V. Description of the invention () 40 First reactor 50 Second reactor (please read the note on the back first) Please fill in this page again for details) 52 Detailed description of the ammonia volatilizer invention The following detailed description only lists the preferred embodiments of the present invention, so as to explain the best mode for implementing the present invention. It should be noted that the present invention can make many improvements and changes. These improvements and changes should still be regarded as the scope of the present invention, so the drawings and detailed description of the present invention are only for the purpose of illustrating the present invention, and the scope of the present invention is not limited to this. Preparation of azidomethanamine according to the present invention, First, urea is pyrolyzed at a temperature higher than the melting point of urea to produce biuret and ammonia of formula 1. In general, biuret is widely used as a precursor for drugs, herbicides, and analytical reagents. It is also widely used as a feed for tooth decay animals, and is widely used in various plastic resin fields. In addition, some biuret derivatives are also known to have the function of physiological healing agents or chemotherapeutics. The following reaction formula 6 shows the heat Production process of biuret by decomposing urea. [Reaction 6] Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economy 9 9 〇〇II il heat II || H2N-C-NH2 + H2N-C-NH2-h2n- c-nh-c-nh2 + nh3 As shown in the reaction formula 6, it can pyrolyze 2 moles of urea and remove ammonia, which can be produced on page 8. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 1237016 A7 B7 V. Description of the invention (biuret. Specifically, as shown in the following reaction formula 7, it is generally assumed that when urea is pyrolyzed, isocyanate and ammonia are first produced, and then the target product, biuret, is produced. [Reaction formula 7] heat H-N = C-0 + NH, please read the meanings on the back first

H-N=c=0 + H2N-C-NH o o II II h2n-c-nh-c-nh2 經濟部智慧財產局員工消費合作社印製 熱解尿素以合成縮二脲之方法的優點在於反應 操作容易’但其缺點則在於尿素轉變成縮二脾的 低’因在生成縮二脲的反應過程中,由於縮二脲 酸間的反應會生成諸如縮三脲及氰尿酸之類的雜 成轉換率過低。如果將反應溫度提高並將反應時 以提高轉換率’則諸如縮三脲及氰尿酸之類的雜 亦會跟著升高。如果降低反應溫度以降低雜質量 速將變慢,使其喪失經濟效益。在本發明中,為 二脲的產率並降低雜質量,反應溫度較好係維持 °C至3 00°c間,且最佳係維持在130°c至i7(rc間 再者,如果將諸如空氣及氮氣這類不會與異氛 的氣體注入反應器中,和/或降低反應器的壓^力 時所生成的副產物-氨,可被有效地自反應器t g 後反應速率會上升,且雜質量也會降低。此夕卜, 第9頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公釐) 簡單且 比例太 與異氰 質,造 間拉長 質濃度 ,反應 提南縮 在 100 酸反應 則反應 除。之 在反應 1237016 Α7 Β7 五、發明説明( 器的高溫下,液相有機化合物可被改變成惰性氣體而可 當作惰性氣體源來使用。 再者’如果必要的話,亦可使用催化劑來提高熱解反 應速率。較佳是使用諸如硝酸、氫氯酸、及硫酸之類的 梁機酸催化劑’諸如亞硫醯氯之類的酸式催化劑,及諸 如轉酸納之類的含硫物質作為催化劑。催化劑的用量較 佳係為每1莫耳尿素約〇. ο ο 1莫耳至0.5莫耳,更佳係為 每1莫耳尿素約0.01莫耳至〇·3莫耳。 下列式2或式3之單齒化縮二脲金屬鹽可藉由讓所得 的縮二膦與次_化金屬化合物或画素與鹼反應來製得。 [式2] Ο 〇 II || Μ 請 先 閲 讀 背 S 之 注 意 事 項 [式3]HN = c = 0 + H2N-C-NH oo II II h2n-c-nh-c-nh2 The method of printing pyrolytic urea to synthesize biuret by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs has the advantage that the reaction operation is easy. However, the disadvantage is that the conversion of urea into bisplenism is low. In the reaction process of biuret formation, due to the reaction between biuret acid, hybrid conversion rates such as triuret and cyanuric acid are too high. low. If the reaction temperature is increased and the conversion rate is increased, the impurities such as triuret and cyanuric acid will also increase. If the reaction temperature is lowered to reduce the amount of impurities, the rate will be slowed down, making it economically ineffective. In the present invention, in order to reduce the yield of diurea and reduce the amount of impurities, the reaction temperature is preferably maintained between ° C and 300 ° c, and the optimal temperature is maintained between 130 ° c and i7 (rc again, if the By-products such as air and nitrogen, which are not injected into the reactor with an atmosphere and / or the pressure of the reactor is reduced, ammonia can be effectively increased from the reactor tg after the reaction rate And the impurity quality will also be reduced. At the same time, page 9 This paper size applies the Chinese National Standard (CNS) A4 specification (210X 297 mm). The ratio is too simple to be isocyanate, and the concentration of elongation is reflected in the reaction. At the reaction of 100% acid, the reaction of Titanium is removed. The reaction is 1237016 A7 B7. 5. Description of the invention (under the high temperature of the device, the liquid-phase organic compounds can be changed to inert gas and can be used as an inert gas source. If necessary, a catalyst may also be used to increase the pyrolysis reaction rate. It is preferable to use a beam acid catalyst such as nitric acid, hydrochloric acid, and sulfuric acid 'an acid-type catalyst such as thionyl chloride, and Sulfur-containing substances such as sodium Catalyst. The amount of the catalyst is preferably about 0.1 to 0.5 mole per 1 mole of urea, and more preferably about 0.01 to 0.3 mole per mole of urea. The following formula 2 Or the bidentate biuret metal salt of formula 3 can be prepared by reacting the obtained biphosphine with a hypo-metal compound or a pixel with a base. [Formula 2] 〇 〇II || Μ Please read the back first Precautions for S [Eq. 3]

ο οL II II H2N-C-N-C-NH 經濟部智慧財產局員工消費合作社印製 在上述式2及式3中,M代表金屬且X代表函素。直 接製備單画化縮二脲金屬鹽的方法係藉由讓縮二腓與次 鹵化金屬化合物如反應式8所示進行反應,明確的實施 第10頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 五、發明説明() 例示於反應式9中。 [反應式8 ] A7 B7 0 0I! I丨 H,N-C-NH-C-NH, +ο ο Printed by II II H2N-C-N-C-NH Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs In the above formulas 2 and 3, M represents a metal and X represents a letter. The method for directly preparing the single-drawing biuret metal salt is carried out by reacting bifurcate with a subhalogenated metal compound as shown in Reaction Formula 8. The paper standard is applicable to Chinese National Standard (CNS) A4 Specifications (210X297 mm) 1237016 V. Description of the invention () An example is shown in reaction formula 9. [Reaction formula 8] A7 B7 0 0I! I 丨 H, N-C-NH-C-NH, +

M0XM0X

0 0II II H W-C-N-C-NH or ο οII II μ N-C-N-C-NH + Η,〇 X Μ0 0II II H W-C-N-C-NH or ο οII II μ N-C-N-C-NH + Η, 〇 X Μ

Μ X 在上述反應式中,Μ代表金屬且X代表齒素。 [反應式9] Ο ο丨I II + NaOClM X In the above reaction formula, M represents a metal and X represents a tooth element. [反应 式 9] 〇 ο 丨 I II + NaOCl

NH oyc-善—α Q=-c- N- 2 HNH oyc- 善 —α Q = -c- N- 2 H

Na or N- 2 Η o=c-a善—Na o=c- ΝΗ ο 2 ΗNa or N- 2 Η o = c-a 善 —Na o = c- ΝΗ ο 2 Η

C f請先閱讀背面之注意事項再碼寫本頁} 經濟部智慧財產局員工消費合作社印製 參照上述反應式9,縮二脲與次氯酸鈉反應形成氣化 縮二脲鈉鹽。因上述反應式係為一放熱反應,反應系統 較佳係維持在低溫下。但所得的氯化縮二脲鈉鹽對中等 程度的讓而言,相當安定,因此可於室溫下進行製備。 較佳的反應溫度是低於60°c,更佳是是介於_10。(:至 °C間,最佳是介於-5 °C至3 5 °C間。在經濟效益及操作設 備的考量下,每1莫耳尿素之次_化金屬的莫耳反應比 例較佳係介於〇. 1至2間。當莫耳反應比例低於1莫耳 時’該過量的縮二脲可被回收並重新使用。在上述反應 第11頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016C f Please read the notes on the back before writing this page} Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs Refer to the above reaction formula 9, biuret reacts with sodium hypochlorite to form a vaporized biuret sodium salt. Since the above reaction system is an exothermic reaction, the reaction system is preferably maintained at a low temperature. However, the obtained sodium biuret chloride is quite stable for a moderate degree of yield, and therefore it can be prepared at room temperature. The preferred reaction temperature is below 60 ° C, and more preferably between -10. (: To ° C, the best is between -5 ° C to 3 5 ° C. In consideration of economic benefits and operating equipment, the molar response ratio of chemical reaction per 1 mole of urea is better It is between 0.1 and 2. When the molar reaction ratio is lower than 1 molar, the excess biuret can be recovered and reused. In the above reaction, page 11 of this paper applies the Chinese national standard (CNS ) A4 size (210X297 mm) 1237016

五、發明説明() 式中,當莫耳反應比例低於〇 1或反應溫度低於_ i 0C時, 反應時間將變得太長。且如果莫耳反應比例高於2以上, 則會使生產成本變高且可能產生副產物。再者,如果反 應溫度在6 0 C以上,該單鹵化縮二脲金屬鹽產物會被分 解,因其在高溫下並不安定。在上述情況下所獲得的氯 化縮二將鈉鹽可直接使用或儲存以用於下一反應。 反應式10示出由縮二脲與_素及鹼反應來製備上述 式2或式3之單鹵化縮二脲金屬鹽的方法。如反應式10 所示’在縮二脲與諸如氯之自素或画素化合物反應後’ 可得單齒化縮二脲(5),至於單齒化縮二脲金屬鹽則只要 添加諸如金屬氫氧化物(如,氫氧化鈉、氫氧化钾、氫氧 化鈣)這類的鹼,到所得的單函化縮二脲(5)中即可製得。 [反應式10] .......—-----訂 (請先閲讀背面之注意事項再填寫本頁) 〇 οιι ιι Η N-C-NH-C-NH + Χ2V. Description of the invention () In the formula, when the molar reaction ratio is lower than 0 1 or the reaction temperature is lower than − i 0C, the reaction time will become too long. And if the Mohr reaction ratio is higher than 2 or more, it will increase the production cost and may produce by-products. Furthermore, if the reaction temperature is above 60 ° C, the monohalogenated biuret metal salt product is decomposed because it is unstable at high temperatures. The sodium bichloride obtained in the above case can be used directly or stored for the next reaction. Reaction formula 10 shows a method for preparing a monohalogenated biuret metal salt of the above formula 2 or 3 by reacting biuret with a prime and a base. As shown in Reaction Formula 10, "After the biuret is reacted with an autogen or a pigment compound such as chlorine", a monodentate biuret (5) can be obtained. As for the monodentate biuret metal salt, only metal hydrogen such as metal hydrogen can be added. Oxide (such as sodium hydroxide, potassium hydroxide, calcium hydroxide) and other bases can be obtained by the obtained monofunctional biuret (5). [反应 式 10] .......—----- Order (Please read the precautions on the back before filling this page) 〇 οιι ιι Η N-C-NH-C-NH + Χ2

Ο Ο II II h2n-c-n-c-nh2 + μοη XΟ Ο II II h2n-c-n-c-nh2 + μοη X

ο ο II II H2N-C-N-C-NH2 -f ΗΧ ' k (5) ο ο II丨I H.N-C-N-C-NH 2 II 經濟部智慧財產局員工消費合作社印製 在上述反應式10中,Μ代表金屬且X代表画素。 該產生單函化縮二脲(5)的反應係為一放熱反應,故反 溫度較好維持在低溫,即60°C以下,較佳係介於-1 〇°C 6〇t間;最佳係介於-5°C至30°C間,以保持穩定的反 第12頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明説明() 應速率及反應的安定性。或者,可藉由先混合金屬氫氧 化物與縮二脾’之後讓_素與所得產物反應,這樣的方 式來製備單函化縮二脲金屬鹽。因此反應亦為放熱反應, 故反應溫度亦應維持在低溫,較佳係介於^至6 〇。匸 間;最佳係介於-51至30。(:間。在上述反應中,當反應 溫度低於1 (TC時,反應時間將拉得太長;若反應溫度高 於6 0 C時,則該單函化縮二脲金屬鹽可能會因為其本身 的熱不安定性而分解。如反應式u所示,所得的單鹵化 縮二脾金屬鹽可以是3-單_化縮二脲金屬鹽(6)或1-單鹵 化縮二脲金屬鹽(7)。 [反應式1 1 ]?\ ?\ MOX h2n-c-nh-c-nh2 + or - 1 2 3 4 5 十 2Λ/Ι0Η (6) (7) 為產生疊氮甲醯胺,讓所得的單函化縮二脲金屬鹽與 熱解尿素時所產生的氨一起反應。一般推測其反應機制 與反應式12所示之費洛斯基反應(Favorskii reaction)或 反應式13所示之霍夫曼重排反應(Hoffman rearrangement reaction)類似 〇 H,ο ο II II H2N-CNC-NH2 -f Η × 'k (5) ο ο II 丨 I HN-CNC-NH 2 II Printed in the above reaction formula 10, M represents the metal and X stands for pixels. The reaction system for generating monofunctional biuret (5) is an exothermic reaction, so the inverse temperature is preferably maintained at a low temperature, that is, below 60 ° C, and preferably between -10 ° C and 60t; The best range is between -5 ° C and 30 ° C, in order to maintain a stable anti-page. This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 1237016 A7 B7 Employees ’Cooperatives, Intellectual Property Bureau, Ministry of Economic Affairs Printed 5. Description of the invention () Response rate and stability of reaction. Alternatively, a monofunctional biuret metal salt can be prepared by first mixing a metal hydroxide with bisplenol 'and then reacting the element with the obtained product. Therefore, the reaction is also an exothermic reaction, so the reaction temperature should also be maintained at a low temperature, preferably between ^ and 60.匸; the best range is -51 to 30. (: Between. In the above reaction, when the reaction temperature is lower than 1 (TC), the reaction time will be too long; if the reaction temperature is higher than 60 ° C, the monofunctional biuret metal salt may be due to It decomposes due to its thermal instability. As shown in Reaction Formula u, the obtained monohalogenated biuret metal salt can be a 3-mono-biuret metal salt (6) or a 1-monohalobiuret metal salt (7). [Reaction formula 1 1]??? MOX h2n-c-nh-c-nh2 + or-1 2 3 4 5 ten 2Λ / Ι0Η (6) (7) In order to produce azidomethanamine, The obtained monofunctional biuret metal salt is reacted with ammonia generated when urea is pyrolyzed. It is generally estimated that the reaction mechanism is the same as the Favorskii reaction shown in Reaction Formula 12 or the reaction shown in Reaction Formula 13. Hoffman rearrangement reaction is similar to 〇H,

0 Ο II II ,Ν-C-N-C-NH_ 1 I 第13頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) (請先閲讀背面之注意事項再響本頁) 本一 0Γ Ο 0 II II h2n-c-n-c-nh 1237016 Λ7 B7 五、發明説明( [反應式1 2 ] Ο 〇 Η 丨I h2n-c-n-c-nh (8) H2N-〇-N^f0 Ο II II, Ν-CNC-NH_ 1 I page 13 This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) (Please read the precautions on the back before ringing this page) Ben 0Γ 〇 0 II II h2n-cnc-nh 1237016 Λ7 B7 V. Description of the invention ([Reaction formula 1 2] 〇 〇Η 丨 I h2n-cnc-nh (8) H2N-〇-N ^ f

H NH.H NH.

〇 II H2N-C-NT ο〇 II H2N-C-NT ο

MX o 〇 II II H2N-C-NH-NH-C-NH2 (請先閲讀背面之注意事項再,寫本頁) 裝· 再本一 [反應式1 3 ]MX o 〇 II II H2N-C-NH-NH-C-NH2 (Please read the precautions on the back before writing this page) Install and repeat this one [Reaction formula 1 3]

ο ο if II H0N-C-N-C-NH ο !l H2N-C^5 :〇 NH3 I? I? H2N-C-NH-NH-C-NH. 、τ 參照上述反應式1 2 ’藉由單齒化縮二脾金屬鹽(8)上 陰離子性氮原子之分子間反應,透過氮-氮鍵的形成及移 除金屬函化物’產生了不穩定的昼氮化物衍生物 (diaziridinone)(9)。該疊氮化物衍生物(9)可輕易地與高 反應性的氨反應,因此可製得疊氮甲醯胺。再者,參照 上述反應式1 3 ’ 一般係假設該單_化縮二脾金屬藥會被 轉變成内含異氰酸酯基囷的化合物,且該已轉變的異氰 酸酯化合物會與高反應性的氨反應,而形成叠氮甲酿胺。 在單函化縮二脲金屬鹽與氨(熱解尿素時之副產物)的 反應’在考f其反應速率及效益下,較佳係將反應遥度 維持在0°C至150°c間,更佳係維持在30°c至i 5〇°C間。 第14頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 鬢 經濟部智慧財產局員工消費合作社印製 1237016 A7 B7 五 發明説明() 當反應溫度低於〇 c寺反應速率將變得太慢以致喪失 經濟效益,但當反應溫度高於15〇t時,將因需重新設 計設備使能承受因氣揮發所產生的高内壓,而造成設備 成本上升。再者,可使用自々系4形怨包名台— 丹| j便 资产栝軋怨氨、液態氨或氫氧化 銨。較佳係使用適量的氨以提高反應速率。每莫耳單卣 化縮二脲金屬藥所需使用的氨量介於t至1000莫耳間, 更佳係介於2至5〇〇莫耳間,最佳係介於5 1 1〇〇莫耳 間》…莫耳氣與1莫耳單自化縮二脾金屬鹽反應外, 過量的氨可被回收:再用於以後的反應中。因使用大量 氨造成反應溫度過咼’可提高反應系统壓力以防止氨被播發。此可改立反應速率及#安 擇焱此』汉。 欢率,且壓力較佳係介於i至 1 00kgf/cm2 〇 依據本發明,以尿素為起始物來製備叠氮甲酿胺的反 應示於反應式此外,依據本發明較佳實施例來製備 疊氮甲醯胺的設備則示於第丨圖中。[反應式14] (請先閲讀背面之注意事項再碼寫本頁) 裝· -訂· 經濟部智慧財產局員工消費合作社印製 ο 2 H2N-C-NH2 + 2MOH + &amp; --- HDCA + 2 MX + 2 H2 0 如第1圖所示,依據本發明較佳實施例來製備疊氮甲 酿胺的設備包含熱解爐1 〇,其係可熱解尿素以獲得縮二 第15頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公釐) 1237016 A7 B7 五、發明説明( 經濟部智慧財產局員工消費合作社印製 脲及氨。熱解爐1 0較佳係包含一氣體注入口 12,其係 可將惰性氣體注入熱解爐1 〇中;或包含多種可降低熱解 爐10内之壓力的手段,以便能輕易地自熱解爐10中將 氨移除。該惰性氣體的例子不限於空氣、氮氣、及可在 熱解爐1 0中被改變成惰性氣體的液態有機化合物,其係 不會與異氰酸反應。 自熱解爐1 0中移除的氨較佳係被供應至氨濃縮器20 中,該氨濃縮器20的功能係用以濃縮來自熱解爐10之 氨及在形成疊氮甲醯胺後仍存在的過量氨。存在於熱解 爐1 0内之縮二脲中,諸如縮三脲及氰尿酸之類的雜質, 可藉由再結晶的手段(包括再結晶器3 0及諸如離心機之 類的脫水器32)將其分離後,再供至第一反應器40中。 純化後的縮二脲被送至第一反應器40中,再與次鹵 化金屬化物(例如,NaOC1)或_素(例如,氯)及驗反應, 產生單齒化縮二脲金屬鹽,並被供至第二反應器5〇中。 戎單_化縮二脲金屬鹽與氨反應後即可生成疊氮甲醯 胺’且該參與反應的氨較佳係由氨濃縮器2 〇來提供。所 得之疊氮甲醯胺及過量的氨會再被導至氨揮發器52中。 氨揮發器52可將過量的氨揮發,該被揮發的氨會再被送 至氨濃縮器20。自過量氨中分離出來的疊氮甲醯胺可藉 由諸如濾紙之類的脫水器5 4來純化。 如第1圖及反應式13所示,依據本發明,可以一連 續製程自尿素起始物來製備疊氮甲醯胺。因此整個製程 係被連續執行,因此可改善製程效率。 第16頁 (請先閲讀背面之注意事項再填寫本頁)ο ο if II H0N-CNC-NH ο! l H2N-C ^ 5: 〇NH3 I? I? H2N-C-NH-NH-C-NH., τ Refer to the above reaction formula 1 2 ' The intermolecular reaction of an anionic nitrogen atom on the bisplenic metal salt (8), through the formation of a nitrogen-nitrogen bond and the removal of the metal functional compound ', produces an unstable diaziridinone (9). The azide derivative (9) can be easily reacted with highly reactive ammonia, and thus azidomethanamine can be produced. In addition, referring to the above reaction formula 1 3 ', it is generally assumed that the mono-bicondensate metal drug will be converted into a compound containing isocyanate hydrazone, and the converted isocyanate compound will react with highly reactive ammonia, And azide methylamine is formed. In the reaction of the monofunctional biuret metal salt with ammonia (a by-product when pyrolyzing urea), in consideration of its reaction rate and benefits, it is preferred to maintain the reaction telemetry between 0 ° C and 150 ° C. More preferably, it is maintained between 30 ° c and i50 ° C. Page 14 This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 印 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 1237016 A7 B7 Five invention instructions () When the reaction temperature is lower than 0 ° C the reaction rate will be It becomes too slow to lose economic benefits, but when the reaction temperature is higher than 15t, the equipment cost will increase due to the need to redesign the equipment to withstand the high internal pressure caused by volatilization of the gas. In addition, you can use the self-propelled four-shaped complaint package platform — Dan | j 便 assets, such as ammonia, liquid ammonia or ammonium hydroxide. It is preferred to use a suitable amount of ammonia to increase the reaction rate. The amount of ammonia required per mole of mono-biuret biuret metal medicine is between t and 1,000 moles, more preferably between 2 and 500 moles, and most preferably between 5 1 and 100. Mole Room ... Except for the reaction of Mole gas with 1 Mole monochemically reduced spleen metal salt, excess ammonia can be recovered: it can be used in subsequent reactions. Excessive reaction temperature due to the use of a large amount of ammonia can increase the pressure of the reaction system to prevent ammonia from being circulated. This can change the reaction rate and # 安 择 焱 此 』汉. The yield and pressure are preferably between i and 100 kgf / cm2. According to the present invention, the reaction for preparing azidomethylamine from urea is shown in the reaction formula. In addition, according to the preferred embodiment of the present invention, The equipment for preparing azidomethoxamine is shown in the figure. [Reaction formula 14] (Please read the precautions on the back before writing this page.) Binding · -Order · Printed by the Consumer Cooperative of Intellectual Property Bureau of the Ministry of Economic Affairs 2 H2N-C-NH2 + 2MOH + &amp; --- HDCA + 2 MX + 2 H2 0 As shown in FIG. 1, the equipment for preparing azidomethacamine according to a preferred embodiment of the present invention includes a pyrolysis furnace 1 0, which can pyrolyze urea to obtain shrinkage. Page 15 This paper size applies Chinese National Standard (CNS) A4 specification (210X 297 mm) 1237016 A7 B7 V. Description of the invention (Urea and ammonia printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. Pyrolysis furnace 10 preferably contains 1 The gas injection port 12 is capable of injecting an inert gas into the pyrolysis furnace 10; or includes various means for reducing the pressure in the pyrolysis furnace 10 so that ammonia can be easily removed from the pyrolysis furnace 10. The Examples of the inert gas are not limited to air, nitrogen, and liquid organic compounds that can be changed to inert gas in the pyrolysis furnace 10, which does not react with isocyanic acid. Ammonia removed from the pyrolysis furnace 10 It is preferably supplied to an ammonia concentrator 20 whose function is to concentrate The ammonia in the pyrolysis furnace 10 and the excess ammonia still present after the formation of azidomethanamine. The biuret present in the pyrolysis furnace 10, impurities such as triuret and cyanuric acid can be obtained by The recrystallization means (including the recrystallizer 30 and the dehydrator 32 such as a centrifuge) separates it and then supplies it to the first reactor 40. The purified biuret is sent to the first reactor. In 40, it is then reacted with a metal halide (for example, NaOC1) or a halogen (for example, chlorine) to produce a monodentate biuret metal salt, which is then supplied to the second reactor 50. Rong Dan _The reaction of biuret metal salt with ammonia can generate azidomethoxamine ', and the ammonia participating in the reaction is preferably provided by an ammonia concentrator 20. The obtained azidomethoxamine and excess ammonia will It is then led to the ammonia volatilizer 52. The ammonia volatilizer 52 can volatilize the excess ammonia, and the volatilized ammonia will be sent to the ammonia concentrator 20. The azidomethanamine separated from the excess ammonia can be borrowed Purified by a dehydrator 5 4 such as filter paper. As shown in FIG. 1 and reaction formula 13, according to the present invention, a continuous process can be performed Urea was prepared starting from methyl acyl azide amines. Thus the entire process train is continuously performed, so the process efficiency can be improved. P. 16 (Read Notes on the back and then fill the page)

1237016 A71237016 A7

五、發明説明() (請先閲讀背面之注意事项再填寫本頁} 此外,因單_化縮二脲金屬鹽與反應副產物_氨反應 (故,使原料用量大幅降低,也間接使生產成本下降。 因此,本發製程透過與較不環保的副產物-氨反應,而可 較環保地來製備疊氮甲醯胺。 以下提供本發明較佳實施例及製造例,幫助讀者了解 本發明。但是,本發明的範疇並不僅限於所述之實施例。 篮造例_:製備输二脇 在四頸圓底燒瓶中注入5〇〇克(8·33莫耳)尿素,劇烈 揽摔’並以表1所示的速率將空氣注入燒瓶底部。同時 進行反應5小時,藉由加熱,將反應溫度維持在14〇°c。 反應完成後,以液體色層分析法分析所得固體之組成, 結果揭示於下表1。 表1 實施例 注入空氣 的速率 (升/分鐘) 尿素量 (重量%) 縮二脲量 (重量%) 氰脲酸及 其他固體量 (重量%) 1 0 62 35 3 2 1 41 55 4 3 2 38 60 2 4 4 37 61 2 經濟部智慧財產局員工消費合作社印製 製造例5-7 :製備縮二脲 基本上依製造例1之方法製備縮二脲’但反應只進行 3小時,且改變反應溫度並將空氣注入速率維持在2升/ 第17頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 A7 B7 五、發明説明() 分鐘。反應完成後’以液體色層分析法分析所仔固體之 組成,結果揭示於下表2。 表2 實施例 反應溫度 ΓΟ 尿素量 (重量%) 縮二脲量 (重量%) 氰脲酸及 其他固體量 (重量%) 4 —----- 150 47 50 3 5 160 38.5 57 4.3 6 170 28 65 7 製造例 8-10 : 基本上依製造例1之方法製備縮二解,但反應在下表 3所示之真空幫浦所致之低壓下進行’代替空氣的注入。 反應完成後,以液體色層分析法分析所得固體之組成, 結果揭示於下表3 ° (請先閲讀背面之注意事項再填寫本頁) -訂· 經濟部智慧財產局員工消費合作社印製 表3 實施例 壓力 (毫米汞拄) 尿素量 (重量%) 縮二脲量 (重量%) 氰脲酸及 其他固體量 (重量%) 8 380 56 50 4 9 190 41.5 55 3.5 10 100 40 57 3 製造例11 -1 3 :製備縮二脲 基本上依製造例1之方法製備縮二脲,但反應係於每 1莫耳尿素〇·〇5莫耳各式催化劑下進行,且將空氣注入 第18頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公釐) ί 1237016 A7V. Description of the invention () (Please read the notes on the back before filling out this page} In addition, the reaction of the mono-biuret metal salt with the reaction by-product _ ammonia (thereby greatly reducing the amount of raw materials, and also indirectly production Cost is reduced. Therefore, this process can produce azidomethanamine more environmentally friendly by reacting with ammonia, a by-product that is less environmentally friendly. The following provides preferred embodiments and manufacturing examples of the present invention to help readers understand the present invention However, the scope of the present invention is not limited to the described examples. Basket Example _: Preparation of two-packed flasks. Inject 500 grams (8.33 moles) of urea into a four-necked round-bottomed flask and vigorously fall. Air was injected into the bottom of the flask at the rate shown in Table 1. The reaction was performed simultaneously for 5 hours, and the reaction temperature was maintained at 14 ° C by heating. After the reaction was completed, the composition of the obtained solid was analyzed by liquid chromatography. The results are shown in the following Table 1. Table 1 Example of the rate of air injection (liters / minute) Amount of urea (% by weight) Amount of biuret (% by weight) Cyanuric acid and other solids (% by weight) 1 0 62 35 3 2 1 41 55 4 3 2 38 60 2 4 4 37 61 2 Printed by Manufacturing Cooperative of Employees of the Intellectual Property Bureau of the Ministry of Economic Affairs Example 5-7: Preparation of biuret Basically the method of manufacturing example 1 is used to prepare biuret 'but the reaction only takes 3 hours, and the reaction temperature is changed and the air is removed. The injection rate is maintained at 2 liters / page 17. The paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 1237016 A7 B7 V. Description of the invention () minutes. After the reaction is completed, it is analyzed by liquid chromatography The composition of the solids, the results are shown in the following Table 2. Table 2 Example reaction temperature ΓΟ Amount of urea (% by weight) Amount of biuret (% by weight) Cyanuric acid and other solids (% by weight) 4 ------ -150 47 50 3 5 160 38.5 57 4.3 6 170 28 65 7 Manufacturing Example 8-10: Basically, the diminution solution was prepared according to the method of Manufacturing Example 1, but the reaction was under the low pressure caused by the vacuum pump shown in Table 3 below. Perform the injection instead of air. After the reaction is completed, the composition of the solid obtained is analyzed by liquid chromatography, and the results are disclosed in the table below 3 ° (Please read the precautions on the back before filling this page) Bureau employee consumer cooperative seal Tab. 3 Example Pressure (mmHg) Urea (wt%) Biuret (wt%) Cyanuric acid and other solids (wt%) 8 380 56 50 4 9 190 41.5 55 3.5 10 100 40 57 3 Manufacturing Example 11 -1 3: Preparation of Biuret Biuret is basically prepared according to the method of Manufacturing Example 1, but the reaction is performed under various types of catalyst per 0.05 mole of urea and air is injected. Page 18 This paper size applies to Chinese National Standard (CNS) A4 (210X 297 mm) ί 1237016 A7

五、發明說明() 速率維持在2升/分鐘。反應完成後,以液體色層分析法 刀析所得固體之組成,結果揭示於下表4。 -—7--- 表 4 貫施例 催化劑 尿素量 (重量%) 縮二脲量 (重量%) 氰脲酸及 其他固體量 (重量%) __21 硫酸 34 62 4 12 鱗酸鈉 36 61 3 13 亞硫醯氯 35 62 3 ΙϋΑ 14:合成氣化縮二脲鈉鹽 在2升的玻璃反應器中裝入423.1克(0.287莫耳)、7% 縮二脲之泥狀溶液,攪摔並冷卻至5。(:。在此反應器中, 加入1 2 %次氯化鈉水溶液,將系統之反應溫度維持在5 °c以下。反應完成後,以碘滴定法及液體色層分析法分 析所得溶液之組成。可用之氯為3.3 7%。相當於產率為 9 8%。 製造例1 5 ··合成氯化縮二脲铷驗 在2升的玻璃反應器中裝入423.1克(0.287莫耳)、7% 縮二膊之泥狀溶液,攪拌並冷卻至5。(:。在此反應器中, 加入223克(0.575莫耳)10.3%之氫氧化鈉水溶液’並加 入20.3克(0.287莫耳)的氯氣,將系統之反應溫度維持在 1 0。(:以下。反應完成後,以碘滴定法及液體色層分析法 分析所得溶液之組成。可用之氯為3. 〇%。相當於產率為 第19頁 本紙張尺度適用中國國家標準(CNS)A4規格(210&gt;&lt; 297公釐) (請先閲讀背面之注意事項再壤寫本頁) -訂· 經濟部智慧財產局員工消費合作社印製 1237016 A7 B7 五、發明説明() 9 8% 〇 1造例1 6 :合成氣化縮二脲鈉鹽 在2升的玻璃反應器中裝入423.1克(0·287莫耳)、7% 縮二脲之泥狀溶液,攪拌並冷卻至5 °C。在此反應器中, 加入20.3克(0.287莫耳)的氯氣,將系統之反應溫度維持 在10 °C以下。在添加完氯氣後,一面添加223克(0.575 莫耳)1 0 · 3 %之氫氧化鈉水溶液,一面劇烈携拌,並維持 反應溫度在5 °C以下。反應完成後’以碟滴定法及液體 色層分析法分析所得溶液之組成。可用之氯為3 〇 〇/。。相 當於產率為9 8 %。 (請先閲4謂背面之注意事項再填寫本頁}V. Description of the invention () The rate is maintained at 2 liters / minute. After completion of the reaction, the composition of the obtained solid was analyzed by liquid chromatography, and the results are shown in Table 4 below. --7 --- Table 4 Amount of urea (wt.%) Of biuret (wt.%) Of cyanuric acid and other solids (wt.%) __21 sulfuric acid 34 62 4 12 sodium scale 36 36 Sulfuryl chloride 35 62 3 ΙϋΑ 14: Synthetic gasification biuret sodium salt. A 2 liter glass reactor was charged with 423.1 g (0.287 mol) of a 7% biuret slurry solution, stirred and cooled. To 5. (:. In this reactor, add a 12% aqueous sodium chloride solution to maintain the reaction temperature of the system below 5 ° C. After the reaction is completed, analyze the composition of the resulting solution by iodometric titration and liquid chromatography. The available chlorine is 3.3 7%. This corresponds to a yield of 98%. Production Example 15 ·· Synthetic Biuret Chloride Test In a 2 liter glass reactor, 423.1 grams (0.287 moles), 7% shrinking mud-like solution, stir and cool to 5. (:. In this reactor, add 223 g (0.575 mol) of 10.3% sodium hydroxide aqueous solution 'and add 20.3 g (0.287 mol) 〇%。 Equivalent to the yield of chlorine, the reaction temperature of the system was maintained at 10. (: below. After the reaction is complete, the composition of the solution obtained is analyzed by iodometric titration and liquid chromatography. The available chlorine is 3.0%. For page 19, this paper size applies the Chinese National Standard (CNS) A4 specification (210 &gt; &lt; 297 mm) (Please read the precautions on the back before writing this page) Printed 1237016 A7 B7 V. Description of the invention () 98% 〇1 Example 16: Synthetic gasification shrinkage A diurea sodium salt was charged in a 2 liter glass reactor with 423.1 g (0.287 mol) of a 7% biuret slurry solution, stirred and cooled to 5 ° C. In this reactor, 20.3 was added Grams (0.287 moles) of chlorine gas to maintain the reaction temperature of the system below 10 ° C. After the chlorine gas was added, 223 grams (0.575 moles) of a 10 · 3% sodium hydroxide aqueous solution was added while vigorously carrying Stir and maintain the reaction temperature below 5 ° C. After the reaction is complete, analyze the composition of the resulting solution by dish titration and liquid chromatography. The available chlorine is 300 /. The equivalent yield is 98% . (Please read the precautions on the back of the 4th chapter before filling out this page}

f 經濟部智慧財產局員工消費合作社印製 頁 20 第 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) ^37016f Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, page 20 This paper size applies to China National Standard (CNS) A4 (210X297 mm) ^ 37016

'發明説明( I施全^卜9:合成疊氮甲醯职: 在2升無菌燒瓶中注入593」克依上述製造例14所 製備的氯化縮二脲鈉鹽,並攪拌冷卻至1〇r。維持反應 溫度在i〇°c以下,一面添加600克(8 8莫耳)25%之液態 氨溶液,一面劇烈攪拌。在各種溫度及時間下進行反應。 待反應完成後,將未反應的氨移除,過濾反應溶液可得 不溶於水之疊氮甲醯胺。其產率經計算後揭示於表5中。 差5 實施例 反應條件(溫度、時 一 1 3〇°C、1小時 2 3〇°C、2小時 一 3 3〇°C、3小時 4 6 0°C、1小時 5 60°C、2小時 6 6(TC、3小時 7 90°C、1小時 8 90°C、2小時 9 90°C、3小時 (請先閲讀背面之注意事項再填寫本頁)'Explanation of the invention (Example 1) 9: Synthetic azide. Job: Inject 593 "of a biseptic urea flask into a 2 liter sterile flask. The sodium biuret chloride salt prepared according to the above Production Example 14 was stirred and cooled to 10%. r. Maintain the reaction temperature below 10 ° C, while adding 600 grams (8.8 mol) of 25% liquid ammonia solution, while vigorously stirring. The reaction is carried out at various temperatures and times. After the reaction is completed, the reaction will be unreacted. The ammonia was removed, and the reaction solution was filtered to obtain azidomethanamine, which is insoluble in water. The yield is calculated and shown in Table 5. Poor 5 Example reaction conditions (temperature, hour-130 ° C, 1 Hour 2 30 ° C, 2 hours 1 330 ° C, 3 hours 4 60 ° C, 1 hour 5 60 ° C, 2 hours 66 (TC, 3 hours 7 90 ° C, 1 hour 8 90 ° C, 2 hours 9 90 ° C, 3 hours (Please read the precautions on the back before filling this page)

經濟部智慧財產局員工消費合作社印製 第21頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐)Printed by the Employees' Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs page 21 This paper size applies to China National Standard (CNS) A4 (210X297 mm)

訂 1237016 A7 B7 五、發明説明() 實施例10-18 :合成疊氮甲醯胺 除了添加表6所示之各種催化劑外,基本上依實施例 4的方法進行合成。待反應完成後,過濾反應溶液可得 不溶於水之叠氮甲酸胺。其產率經計算後揭示於表6中。 表6 實施例 所使用的催化劑 產率(%) 10 ZnCl3 94 11 Zn(OH)2 92 12 A1C13 90 13 B aC 12 91 14 CdCl2 92 15 ZnS04 93 16 ZnCl2 + A1C13(各 0.025 莫耳) 96 17 ZnCl2 + BaCl2(各 0.025 莫耳) 94 18 ZnCl2 + CdCl2(各 0.025 莫耳) 96 請 先 閲 讀 背 面 -C 意 事 項 再 填 寫 本 頁 經濟部智慧財產局員工消費合作社印製 第22頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公釐) 1237016 A7 B7 五、發明説明( 實施例19·27 :合成i氮甲醯脸 在2升無菌燒瓶中注入593.1克依上述製造例 〇所 製備的氯化縮二膊鈉鹽’並攪拌冷卻至1 〇 °c。綸杜 唯符反應 溫度在10°C以下,一面添加600克(8·8莫耳)25%之液態 氨溶液,一面劇烈攪拌。在各種溫度及時間下進行反應。 待反應完成後’將未反應的氨移除,過遽反鹿溶液可得 不溶於水之疊氮甲醯胺。其產率經計算後揭示於表7中。 表7Order 1237016 A7 B7 V. Description of the invention () Example 10-18: Synthesis of azidomethoxamine In addition to adding various catalysts shown in Table 6, the synthesis was basically carried out according to the method of Example 4. After the reaction is completed, the reaction solution is filtered to obtain amine azide insoluble in water. The yield is calculated and shown in Table 6. Table 6 Catalyst yield (%) used in the examples 10 ZnCl3 94 11 Zn (OH) 2 92 12 A1C13 90 13 B aC 12 91 14 CdCl2 92 15 ZnS04 93 16 ZnCl2 + A1C13 (0.025 moles each) 96 17 ZnCl2 + BaCl2 (0.025 moles each) 94 18 ZnCl2 + CdCl2 (0.025 moles each) 96 Please read the notice on the back -C before filling out this page. Printed by the Employees ’Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. Page 22 This paper applies to China National Standard (CNS) A4 specification (210X 297 mm) 1237016 A7 B7 V. Description of the invention (Example 19 · 27: Synthetic i-nitrocarbamate face) In a 2 liter sterile flask, 593.1 g prepared according to the above-mentioned manufacturing example 0 was injected. Chlorinated sodium bisulfate 'and stirred to cool to 10 ° C. The reaction temperature of Lu Duweifu is below 10 ° C. While adding 600 g (8.8 mole) 25% liquid ammonia solution, stir vigorously The reaction is carried out at various temperatures and times. After the reaction is completed, the unreacted ammonia is removed, and the water-insoluble azidomethanamine can be obtained by anti-deer solution. The yield is calculated and shown in Table 7 Table 7

經濟部智慧財產局員工消費合作社印製 實施例 反應條件(溫度、時間) 產率(%) 19 3〇°C、1小時 78 20 3 0°C、2小時 89 21 30°C、3小時 89 22 6 0°C、1小時 88 23 60°C、2小時 90 24 60°C、3小時 90 25 90°C、1小時 87 26 90°C、2小時 86 27 90°C、3小時 89 __ 頁 23 第 本紙張尺度適用中國國家標準(CNS)A4規格(210X 297公釐) ) 訂· ί 1670 3 12 五 A7 B7 發明說明() 列28-36:合成疊氣,甲醯胺 除了添加表8所示之各種催化劑外(〇 . 0 5莫耳),基本 上依實施例22的方法進行合成。待反應完成後,將未反 應的氨移除,過濾反應溶液可得不溶於水之疊氮甲醯胺。 其產率經計算後揭示於表8中。 表8 先 閲 讀 背 面 之 注 意 事 項 再 填 寫 本 頁 經濟部智慧財產局員工消費合作社印製 第24頁 實施例 ----- 所使用的催化劑 產率(%) __28 ZnCl3 94 Zn(OH)2 91 30 A1C13 89 31 BaCl2 91 32 CdCl2 93 33 ZnS04 92 34 ZnCl2 + A1C13(各 0.025 莫耳) 97 35 ZnCl2 + BaCl2(各 0.025 莫耳) 93 36 ZnCl2 + CdCl2(各 0.025 莫耳) 96 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 A7 B7 五、發明説明() 實施例37-45 :合成疊氮 在2升操菌燒瓶中注入5 9 3 · 1克依上述製造例1 6所 製備的氯化縮二P鈉鹽,並攪拌冷卻至10X:。維持反應 溫度在l〇°C以下,一面添加600克(8 8莫耳)25%之液態 氨溶液,一面劇烈攪拌。在各種溫度及時間下進行反應。 待反應完成後,將未反應的氨移除,過濾反應溶液可得 不溶於水之疊氮甲驢胺。其產率經計算後揭示於表9中。 表9 經濟部智慧財產局員工消費合作社印製 實施例 反應條件(溫度、時間) 產率(%) 37 3〇°C、1小時 79 38 3 0 C、2小時 88 39 3 0 C、3小時 89 40 60°C、1小時 89 41 6 0 C、2小時 90 42 6 0°C、3小時 91 43 90°C、1小時 88 44 90°C、2小時 88 45 90°C、3小時 89 第25頁 本紙張尺度適用中國國家標準(CNS)A4規格(210Χ 297公釐) (請先閲讀背面之注意事項再填寫本頁) -、τ 1237016 五、發明説明( :合成 除了添加表10所示之各種催化劑外(〇 〇5莫耳卜基 本上依實施例40的方法進行合成。待反應完成後,將未 反應的氨移除,過濾反應溶液可得不溶於水之疊氮甲醯 胺。其產率經計算後揭示於表丨〇中。 表10 產率 (請先閲讀背面之注意事項再填寫本頁)Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. Example Response conditions (temperature, time) Yield (%) 19 30 ° C, 1 hour 78 20 3 0 ° C, 2 hours 89 21 30 ° C, 3 hours 89 22 6 0 ° C, 1 hour 88 23 60 ° C, 2 hours 90 24 60 ° C, 3 hours 90 25 90 ° C, 1 hour 87 26 90 ° C, 2 hours 86 27 90 ° C, 3 hours 89 __ Page 23 This paper size applies the Chinese National Standard (CNS) A4 specification (210X 297 mm). Order · ί 1670 3 12 Five A7 B7 Description of the invention () Column 28-36: Synthetic gas, in addition to formamide The various catalysts shown in Figure 8 (0.05 moles) were synthesized basically according to the method of Example 22. After the reaction is completed, unreacted ammonia is removed, and the reaction solution is filtered to obtain water-insoluble azidomethanamine. The yield is calculated and shown in Table 8. Table 8 Read the notes on the back before filling out this page Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs on page 24 Example ----- Yield of catalyst used (%) __28 ZnCl3 94 Zn (OH) 2 91 30 A1C13 89 31 BaCl2 91 32 CdCl2 93 33 ZnS04 92 34 ZnCl2 + A1C13 (0.025 mol each) 97 35 ZnCl2 + BaCl2 (0.025 mol each) 93 36 ZnCl2 + CdCl2 (0.025 mol each) 96 This paper is applicable to China National Standard (CNS) A4 specification (210X297 mm) 1237016 A7 B7 V. Description of the invention () Examples 37-45: Synthetic azide was injected into a 2 liter bacteria-control flask 5 9 3 · 1 g according to the above-mentioned manufacturing example 16 The prepared sodium salt of bisphosphonium chloride was cooled to 10X with stirring. While maintaining the reaction temperature below 10 ° C, 600 g (8.8 mol) of 25% liquid ammonia solution was added while vigorously stirring. The reaction is carried out at various temperatures and times. After the reaction is completed, unreacted ammonia is removed, and the reaction solution is filtered to obtain water-insoluble azidomethamine. The yield is calculated and shown in Table 9. Table 9 Example printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. Reaction conditions (temperature, time) Yield (%) 37 30 ° C, 1 hour 79 38 3 0 C, 2 hours 88 39 3 0 C, 3 hours 89 40 60 ° C, 1 hour 89 41 6 0 C, 2 hours 90 42 6 0 ° C, 3 hours 91 43 90 ° C, 1 hour 88 44 90 ° C, 2 hours 88 45 90 ° C, 3 hours 89 Page 25 This paper size applies Chinese National Standard (CNS) A4 specification (210 × 297 mm) (Please read the precautions on the back before filling this page)-, τ 1237016 V. Description of the invention (: In addition to the addition of Table 10 The various catalysts shown below (0.05 moles were synthesized basically according to the method of Example 40. After the reaction was completed, unreacted ammonia was removed, and the reaction solution was filtered to obtain water-insoluble azidomethanamine The yield is calculated and shown in Table 丨 〇. Table 10 Yield (please read the notes on the back before filling this page)

Order

經濟部智慧財產局員工消費合作社印製 頁 26第 實施例 所使用的催化劑 46 ZnCl3 93 47 Zn(〇H)2 48 A1C1, 90__ 49 BaCl, 50 CdCl, _- 51 ZnS04 52 ZnCl2 + A1C13(各 0.025 莫耳、 53 ' --------—___ ZnCl2 + BaCl2(各 0.025 莫耳) 54 ZnCl2 + CdCl2(各 0.025 莫耳、 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) τ-r 70 3 12 6 、1 明 發 Λ 五The catalyst used by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, page 26, the catalyst used in the first example 46 ZnCl3 93 47 Zn (〇H) 2 48 A1C1, 90__ 49 BaCl, 50 CdCl, _- 51 ZnS04 52 ZnCl2 + A1C13 (each 0.025 Moore, 53 '------------___ ZnCl2 + BaCl2 (0.025 moles each) 54 ZnCl2 + CdCl2 (0.025 moles each, this paper size applies Chinese National Standard (CNS) A4 specifications (210X297 mm ) τ-r 70 3 12 6 、 1 Mingfa Λ 5

4備度液應可 1 製溫溶反液表 實 :2升無菌燒瓶中注入5933克依上述製造例14所 的氣化縮二膊鈉鹽,並攪拌冷卻至1(rc。維持反應 在lot以下,一面添加表n所示各含量之液態氨 ,—面劇烈攪拌1小時。在各種溫度及時間下進行 待反應完成後’將未反應的氨移除,過濾反應溶 得不溶於水之疊氮甲醯胺。其產率經計算後揭示於 中。 表114 The preparation solution should be able to produce 1 temperature-soluble reaction liquid. In a 2 liter sterile flask, inject 5933 grams of the vaporized sodium bisulfate according to the above-mentioned manufacturing example 14, and stir to cool to 1 (rc. Maintain the reaction in the lot. Next, while adding liquid ammonia of each content shown in Table n, the mixture is vigorously stirred for 1 hour. After the reaction is completed at various temperatures and times, the unreacted ammonia is removed and the reaction is filtered to obtain a water-insoluble stack. Azamethoxamine. Its yield is calculated and shown in Table 11. Table 11

包例 — 丨6 叉 ;8 氨與氣化縮二將納鹽 之莫耳比例(%) 產率(%) 15 75 30 87 60 90 90 89 @Ll9-62 :合成疊氮甲醯眩 缝濟部智慧財產局員工消費合作社印製 在 備度、添面拌 製溫所一攪 2升無菌燒瓶中注入5 93 · 1克依上述製造例1 4所 的氯化縮二脲鈉鹽,並攪拌冷卻至10。(:。維持反應 &amp; 1 0 °C以下,一面添加表1 2所示各種有機溶劑, 力口量為水重的0.5倍。維持反應溫度在i〇°c以下, 添加600克(8.8莫耳)25%之液態氨溶液,一面劇烈 1小時。在各種溫度及時間下進行反應。待反應完 第27頁 本紙張尺度適用中國國家標準(CNS)A4規格(210Χ297公釐) 1237016Cases — 丨 6 forks; 8 Molar ratio of ammonia and gasification shrinkage sodium salt (%) Yield (%) 15 75 30 87 60 90 90 89 @ Ll9-62: Synthetic azide The Consumer Cooperative of the Ministry of Intellectual Property Bureau printed 593 · 1 g of the sodium biuret chloride according to the above-mentioned manufacturing example 14 into a 2 liter sterile flask prepared by the preparation and flour mixing and heating plant, and stirred Cool to 10. (: Maintain the reaction &amp; below 10 ° C, while adding various organic solvents shown in Table 12, the volume is 0.5 times the weight of water. Maintain the reaction temperature below i0 ° c, add 600 grams (8.8 Mo) Ear) 25% liquid ammonia solution, one side is violent for 1 hour. The reaction is performed at various temperatures and times. After the reaction is completed, page 27 This paper applies the Chinese National Standard (CNS) A4 specification (210 × 297 mm) 1237016

、發明説明( 五 成後 之ί V丸π味迥嫕反應溶液可得 亂甲醯胺。其產率經計算後揭示於表12中 實j 5 6 一- 6 6 丄 2 表12 所使用的溶劑 ^ ~------ 產率(%) 甲醇 90 二曱基甲醯胺 ~ __ 94 四氫呋喃 -——-__ 一— ---—------ 90 乙腈 —-—^_ --- 88 ---- 如 町以 燊氮 將副 濟、 化, 經濟部智慧財產局員工消費合作社印製 上述,依據本發明製備疊氮甲酿胺之方法及投備, 價格便宜且可輕易取得的尿素作為起始#,來製備 甲綠胺。此外,本發明亦因使用副產物作為原料而 產物量降至最低’且使用有效的連續製帛,而可經 環保地來製備疊氮甲酿胺。 .述僅為本發明之詳細說明,需知本發明可有各種變 這些變化及改良應仍視為屬於本發明之範轉。 第28頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐)Description of the invention (50% of the 丸 V pill 味 taste 嫕 嫕 reaction solution can be obtained ranformamidine. The yield is calculated and shown in Table 12. j 5 6 1-6 6 丄 2 Table 12 Solvent ^ ~ ------ Yield (%) Methanol 90 Dimethylformamide ~ __ 94 Tetrahydrofuran --- ---__ One---- ------- 90 Acetonitrile ----- ^ _ --- 88 ---- For example, the above-mentioned method and preparation for the preparation of azidomethanamine according to the present invention are prepared by the consumer cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs and the Ministry of Economic Affairs of the Intellectual Property Bureau of the Ministry of Economic Affairs. Urea, which is easily obtained, is used as the starting # to prepare methyl green amine. In addition, the present invention also uses by-products as raw materials to minimize the amount of the product, and uses an effective continuous process to produce azide, which can be used to prepare azide in an environmentally friendly manner. Methylamine. The description is only a detailed description of the present invention. It should be noted that the present invention can have various changes. These changes and improvements should still be regarded as a paradigm shift of the present invention. Page 28 This paper applies the Chinese National Standard (CNS) A4 size (210X297 mm)

Claims (1)

1237016 y,V A:- B3 C8 D8 第仍號專利案P年S月修正 申請專 1利策1237016 y, V A:-B3, C8, D8, No. P patent, amended in September, P. 'i 1. 一種製備疊氮甲醯胺的方法,其係包含下列步騾: 熱解尿素以獲得式1之縮二脲及氨; [式1] 〇 〇 II Η II Η2Ν一C—N—C一ΝΗ2 讓所得之縮二脲與次i化金屬化合物或i素及鹼 反應,以獲得式2或式3之單_化縮二脲金屬鹽;[式2] 〇 Ο II II H2N—C一 N-C-NH X Μ (請先閲讀背面之注意事項再塡寫本頁) •、一一云 [式3] Ο 〇 II II H2N-C-N-C—ΝΗ Μ X 線 經 濟 部 智 慧 財 產 局 貝 X 消 費 合 作 社 印 製 在式2及式3中,Μ代表金屬且X代表鹵素; 讓所得之單_化縮二脲金屬鹽與包含來自熱解尿 素時所產生的氨反應,且該單_化縮二脲金屬鹽與總 氨量之莫耳比係介於1 : 1至1 : 1000間。 2.如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中熱解尿素之溫度係介於l〇〇°C至300°C間。 第29頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) 1237016 B8 C8 D3 六、申請專利範圍 3 .如申請專利範圍第1項所述製備疊氮甲醯胺之方法, (請先閱讀背面之注意事項再填寫本頁) * 其中在執行該熱解尿素反應時,同時將氨自反應系統 内移除。 4. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中在執行該熱解尿素反應時,同時還可進行注入惰 性氣體的製程和/或降低系統壓力的製程。 5. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中該熱解尿素反應係於至少一種催化劑存在下進 行,該催化劑係選自無機酸催化劑、和酸式催化劑、 及包含磷在内的物質所組成的族群中。 6. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中縮二脲與次函化金屬化合物的莫耳比介於1 : 〇. 1 至1 : 2間。 經 濟 部 智 慧 財 產 局 員 X 消 費 合 作 社 印 製 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中之單化縮二腓金屬鹽係藉由混合金屬氫氣化物 與式1之縮二脲並接著讓所得產物與素反應而製 得,或讓式1之縮二腿與iS素氣體反應後再讓所得產 物與鹼反應後而製得。 第30頁 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐) «888 CBCD 1237016 六、申請專利範圍 8. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中獲得單鹵化縮二脲金屬鹽的製程係於60°C以下的 溫度進行。 9. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中之氨係指液態氨、氨氣或銨水。 10. 如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中單鹵化縮二脲金屬鹽與氨之反應係於〇°C至150 °c的溫度範圍内進行。 1 1.如申請專利範圍第1項所述製備疊氮甲醯胺之方法, 其中之反應溶劑係由水及一第二種溶劑組成之混合 物,該第二種溶劑為一極性溶劑,其係選自由水、甲 醇、乙醇、丙醇、異丙醇及其混合物所組成的族群中; 或是該第二種溶劑為一非質子型溶劑,其係選自由二 曱基甲醯胺、二甲基亞颯、二甲基乙醯胺及其混合物 所組成的族群中。 1 2. —種製備疊氮甲醯胺的設備,其係包含: 一熱解爐,其係可熱解尿素以獲得縮二服及氨; .一再結晶器,其係可純化獲自熱解爐中的縮二脲; 一第一反應器,其係可讓縮二膦與次i化金屬化 合物反應或讓縮二脲與_素及鹼反應而製得單卣化縮 第31頁 本紙張尺度適用申國國家標準(CNS)A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) --5T» 線-*&gt; 經 濟 部 智 慧 財 產 局 員 X 消 費 合 作 社 印 製 5 8 8 8 :BCD 1237016 六、申請專利範圍 二脲金屬鹽; 一第二反應器,其係可讓單iS化縮二脲金屬鹽與 氨反應而合成疊氮甲酸胺;及 一氨揮發器,其係可將過量的氨與疊氮甲醯胺分 開來,並將所分離出來的氨供至氨濃縮器中,其中之 氨濃縮器可濃縮過量的氨及來自熱解爐中的氨’且可 將該已濃縮的氨供至第二反應器中。 1 3.如申請專利範圍第1 2項所述製備疊氮曱醯胺之設備, 其中之熱解爐具有一可供注入惰性氣體的氣體注入 口,該惰性氣體係不會與熱解爐中的異氰酸反應。 1 4,如申請專利範圍第1 2項所述製備疊氮甲醯胺之設備, 其中之熱解爐具有一種可降低壓力以移除熱解爐中之 氨的裝置。 (請先閱讀背面之注意事項再填寫本頁) 、τ 線乘 經濟部智慧財產局員工消費合作社印製 頁 32 第 本紙張尺度適用中國國家標準(CNS)A4規格(210X297公釐)'i 1. A method for preparing azidomethoxamine, which comprises the following steps: Pyrolysis of urea to obtain biuret and ammonia of formula 1; [Formula 1] 〇〇II Η II Η2Ν-C-N- C-ΝΗ2 reacts the obtained biuret with a secondary metal compound or element and a base to obtain a mono-biuret metal salt of formula 2 or formula 3; [Formula 2] 〇II II H2N-C One NC-NH X Μ (Please read the notes on the back before writing this page) • One and one cloud [Formula 3] 〇 Ⅱ II H2N-CNC-NΗ Μ X-ray Ministry of Economy Intellectual Property Bureau Bei X Consumer Cooperative Printed in Formulas 2 and 3, M represents a metal and X represents a halogen; the resulting mono-biuret metal salt is allowed to react with ammonia generated when the urea is derived from pyrolysis, and the mono-biuret The molar ratio of metal salt to total ammonia is between 1: 1 and 1: 1000. 2. The method for preparing azidomethoxamine according to item 1 of the scope of the patent application, wherein the temperature of the pyrolyzed urea is between 100 ° C and 300 ° C. Page 29 This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 1237016 B8 C8 D3 VI. Application for patent scope 3. The method for preparing azidomethoxamine as described in item 1 of the patent scope, ( Please read the notes on the back before filling this page) * Among them, ammonia is removed from the reaction system when performing the pyrolysis urea reaction. 4. The method for preparing azidomethoxamine as described in item 1 of the scope of the patent application, wherein when performing the pyrolysis urea reaction, a process of inert gas injection and / or a process of reducing system pressure can be performed at the same time. 5. The method for preparing azidomethoxamine according to item 1 of the scope of the patent application, wherein the pyrolysis urea reaction is performed in the presence of at least one catalyst selected from the group consisting of an inorganic acid catalyst and an acid catalyst, and In a group of substances including phosphorus. 6. The method for preparing azidomethoxamine as described in item 1 of the scope of the patent application, wherein the molar ratio of the biuret to the hypothesizing metal compound is between 1: 0.1 and 1: 2. Member of the Intellectual Property Bureau of the Ministry of Economic Affairs, X Consumer Cooperative, printed the method for preparing azidomethoxamine as described in item 1 of the scope of patent application, in which the singulated bifurcate metal salt is obtained by mixing the metal hydride with the biform of formula 1 Urea is then prepared by reacting the resulting product with a prime, or by reacting the two legs of Formula 1 with an iS prime gas and then reacting the resulting product with a base. Page 30 This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) «888 CBCD 1237016 6. Application for patent scope 8. The method for preparing azidomethoxamine as described in item 1 of the patent scope, where The process for obtaining the monohalogenated biuret metal salt is performed at a temperature below 60 ° C. 9. The method for preparing azidomethoxamine as described in item 1 of the scope of patent application, wherein ammonia means liquid ammonia, ammonia gas or ammonium water. 10. The method for preparing azidomethoxamine as described in item 1 of the scope of the patent application, wherein the reaction between the monohalogenated biuret metal salt and ammonia is performed at a temperature ranging from 0 ° C to 150 ° C. 1 1. The method for preparing azidomethoxamine as described in item 1 of the scope of patent application, wherein the reaction solvent is a mixture of water and a second solvent, and the second solvent is a polar solvent, which is Selected from the group consisting of water, methanol, ethanol, propanol, isopropanol, and mixtures thereof; or the second solvent is an aprotic solvent, which is selected from the group consisting of dimethylformamide and dimethylformamide In the group consisting of sulfoximine, dimethylacetamide and mixtures thereof. 1 2. A device for preparing azidomethoxamine, which comprises: a pyrolysis furnace, which can pyrolyze urea to obtain shrinkage and ammonia; a recrystallizer, which can be purified and obtained from pyrolysis Biuret in the furnace; a first reactor, which can make bipyridine react with secondary metal compounds or biuret with _ prime and alkali to produce mono-condensation page 31 of this paper Standards apply to the National Standard (CNS) A4 specification (210X297 mm) (Please read the precautions on the back before filling out this page) --5T »Line-* &gt; Member of the Intellectual Property Bureau of the Ministry of Economy X Printed by Consumer Cooperatives 5 8 8 8: BCD 1237016 VI. Patent application scope Diurea metal salt; a second reactor, which is capable of reacting a single iS biuret metal salt with ammonia to synthesize amine azide; and an ammonia volatilizer, which The system can separate excess ammonia from azidomethoxamine and supply the separated ammonia to an ammonia concentrator, where the ammonia concentrator can concentrate the excess ammonia and ammonia from the pyrolysis furnace. This concentrated ammonia was supplied to a second reactor. 1 3. The equipment for preparing azidoamine as described in item 12 of the scope of the patent application, wherein the pyrolysis furnace has a gas injection port for injecting inert gas, and the inert gas system will not interact with the pyrolysis furnace. Isocyanate reaction. 14. The apparatus for preparing azidomethoxamine as described in item 12 of the scope of the patent application, wherein the pyrolysis furnace has a device capable of reducing the pressure to remove ammonia in the pyrolysis furnace. (Please read the precautions on the back before filling out this page), τ LINE LINE Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economy
TW091100904A 2001-10-24 2002-01-21 Method and apparatus for preparing hydrazodicarbonamide using urea as starting material TWI237016B (en)

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US4654441A (en) * 1980-08-15 1987-03-31 Moorman Manufacturing Company Biuret production by controlled pyrolysis of urea
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