JP2014031284A - Production method of rdx - Google Patents

Production method of rdx Download PDF

Info

Publication number
JP2014031284A
JP2014031284A JP2012171562A JP2012171562A JP2014031284A JP 2014031284 A JP2014031284 A JP 2014031284A JP 2012171562 A JP2012171562 A JP 2012171562A JP 2012171562 A JP2012171562 A JP 2012171562A JP 2014031284 A JP2014031284 A JP 2014031284A
Authority
JP
Japan
Prior art keywords
rdx
dissolved
solution
production method
subjected
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.)
Granted
Application number
JP2012171562A
Other languages
Japanese (ja)
Other versions
JP5993241B2 (en
Inventor
Yoshiharu Yokote
義治 横手
Tsuneo Yamamoto
恒夫 山本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chugoku Kayaku KK
Original Assignee
Chugoku Kayaku KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chugoku Kayaku KK filed Critical Chugoku Kayaku KK
Priority to JP2012171562A priority Critical patent/JP5993241B2/en
Publication of JP2014031284A publication Critical patent/JP2014031284A/en
Application granted granted Critical
Publication of JP5993241B2 publication Critical patent/JP5993241B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

PROBLEM TO BE SOLVED: To provide a production method of RDX in which a content of HMX is made few, thereby fastening of a crystal of the HMX to an inner wall of a crystallization tank is made few, and secular change of impact sensitivity is made few.SOLUTION: A production method of RDX is configured such that a solution in which ammonium nitrate is dissolved in concentrated nitric acid, a solution in which hexamethylene tetramine is dissolved in acetic acid, and acetic acid anhydride are made a raw material, the raw material is performed by nitration, then added by water to be subjected to hydrolysis, subjected to filtration to separate waste acid, then subjected to water washing, next crude RDX obtained by performing wash boiling is dissolved by an organic solvent to perform crystallization, performed by water washing, then is filtered to perform recrystallization, and the production method of RDX is characterized in that a particle of 74-125 μm in the RDX subjected to crude crystallization and/or recrystallization is removed.

Description

本発明は、爆薬組成物の主成分であるヘキソーゲン(以下、RDXという)の製造方法に関する。   The present invention relates to a method for producing hexogen (hereinafter referred to as RDX) which is a main component of an explosive composition.

RDXの製造方法の一つに酢酸法がある。この方法は図1に示すように、硝酸アンモニウムを濃硝酸に溶解させた溶液と、ヘキサメチレンテトラミン(ヘキサミン)を酢酸に溶解させた溶液と、無水酢酸を原料とし、これをニトロ化したのち水を加えて加水分解し、ろ過して廃酸を分離したのち水洗し、ついで煮洗して得られた粗RDXを有機溶媒で溶解して晶出し、水洗後ろ過して再結晶したRDXを得ることよりなるもので、この方法により得られたRDXにはオクトーゲン(以下、HMXという)が規格上4〜15%(適用規格:TL-1376-802)含まれている。   One method for producing RDX is the acetic acid method. In this method, as shown in FIG. 1, a solution in which ammonium nitrate is dissolved in concentrated nitric acid, a solution in which hexamethylenetetramine (hexamine) is dissolved in acetic acid, and acetic anhydride as a raw material are nitrated. In addition, hydrolysis, filtration to separate the waste acid, followed by washing with water, followed by boiling and washing to obtain a crude RDX dissolved in an organic solvent, crystallization, washing with water and filtration to obtain recrystallized RDX The RDX obtained by this method contains octogen (hereinafter referred to as HMX) 4 to 15% (applicable standard: TL-1376-802) according to the standard.

近年、高エネルギー化と安全性を高めるため、ニトラミン系発射薬の開発が進められているが、発射薬原料として酢酸法によるRDXを用いた場合、RDXを溶媒法で細粒化する際、溶媒によっては、溶解度がRDXよりHMXのほうが低いため、晶析する際にHMXの結晶が晶析装置にRDXより先に析出して、晶析槽内壁への固着の原因となり、作業効率が悪くなる。また、衝撃感度が鈍感化された酢酸法RDXでも含有するHMX分が原因となり、衝撃感度の経年変化が起こりやすくなる、との報告もあり、RDX中のHMXが減少すれば、経年変化が生じにくくなる可能性が高くなると考えられる。   In recent years, development of nitramine-based propellants has been promoted in order to increase energy and safety, but when RDX by the acetic acid method is used as a propellant raw material, Depending on the type, the solubility of HMX is lower than that of RDX, so that when crystallizing, HMX crystals are precipitated in the crystallizer before RDX, causing sticking to the inner wall of the crystallization tank, resulting in poor working efficiency. . Also, there is a report that the HMX content contained even in the acetic acid method RDX in which the impact sensitivity is desensitized causes the secular change of the impact sensitivity to occur, and if the HMX in the RDX decreases, the secular change will occur. It is thought that the possibility of becoming difficult becomes high.

本発明は、かかる点に鑑みてなされたもので、HMX分の少ないグレードのRDXの製造方法を提供することを目的とする。   This invention is made | formed in view of this point, and it aims at providing the manufacturing method of RDX of a grade with few HMX content.

本発明者らは、粗結晶及び再結晶品のRDXについてそれぞれ粒度別にHMX含有量を測定した。   The inventors of the present invention measured the HMX content for each grain size of the RDX of the crude crystal and the recrystallized product.

表1及び図2は、粗結晶RDXのサンプル1−3における粒度分布ごとのHMX含有量(%)を示すものであり、表2及び図3は再結晶RDXのサンプル1−3における粒度分布ごとのHMX含有量(%)を示すものである。   Table 1 and FIG. 2 show the HMX content (%) for each particle size distribution in the sample 1-3 of the crude crystal RDX, and Table 2 and FIG. 3 show each particle size distribution in the sample 1-3 of the recrystallized RDX. This shows the HMX content (%).

以上の測定結果より本発明者らは、粗結晶品及び再結晶品のRDXはいずれも粒度が74〜125μm以下、とくに74μm以下においてHMX含有量が高いことを見出した。   From the above measurement results, the present inventors have found that the RDX of the crude crystal product and the recrystallized product has a high HMX content when the particle size is 74 to 125 μm or less, particularly 74 μm or less.

本発明は、かかる知見に基づいてなされたもので、硝酸アンモニウムを濃硝酸に溶解させた溶液と、ヘキサミンを酢酸に溶解させた溶液と、無水酢酸を原料とし、これをニトロ化したのち水を加えて加水分解し、ろ過して廃酸を分離したのち水洗し、ついで煮洗して得られた粗RDXを有機溶媒で溶解して晶出し、水洗後ろ過して再結晶することよりなるRDXの製造方法において、粗結晶及び若しくは再結晶されたRDXのうち、74〜125μm以下、好ましくは74μm以下の粒子を除去することを特徴とする。   The present invention has been made on the basis of such knowledge. A solution in which ammonium nitrate is dissolved in concentrated nitric acid, a solution in which hexamine is dissolved in acetic acid, acetic anhydride as a raw material, which is nitrated and added with water. Hydrolyzed, separated by filtration and washed with water, then boiled and washed to dissolve the crude RDX with an organic solvent, crystallized, washed with water, filtered and recrystallized. In the production method, particles of 74 to 125 μm or less, preferably 74 μm or less, are removed from the crude crystals and / or recrystallized RDX.

本発明方法によると、HMX分が4%未満のRDXを得ることができる。   According to the method of the present invention, RDX having an HMX content of less than 4% can be obtained.

従来の酢酸法RDX製造方法を示すフロー図。The flowchart which shows the conventional acetic acid method RDX manufacturing method. 粗結晶品の粒度分布ごとのHMX含有量を示すグラフ。The graph which shows HMX content for every particle size distribution of a coarse crystal product. 再結晶品の粒度分布ごとのHMX含有量を示すグラフ。The graph which shows HMX content for every particle size distribution of a recrystallized product. 本発明に係るRDX製造方法を示すフロー図。The flowchart which shows the RDX manufacturing method which concerns on this invention.

図4は、本発明に係るRDXの製造方法を示すもので、図1に示す従来方法と異なる点は、粗RDX製造後、粗RDXを分級して74〜125μm以下、とくに74μm以下の粒子を除去する工程を新たに設けた点で、篩上の粗RDXを従来法と同じ工程にて再結晶化処理してなるものである。   FIG. 4 shows a method for producing RDX according to the present invention. The difference from the conventional method shown in FIG. In the point which newly provided the process to remove, the coarse RDX on a sieve is recrystallized in the same process as the conventional method.

本実施形態の製造法によると、HMX含有量が0.5〜1.2%のRDXを得ることができる。   According to the production method of the present embodiment, RDX having an HMX content of 0.5 to 1.2% can be obtained.

Claims (2)

硝酸アンモニウムを濃硝酸に溶解させた溶液と、ヘキサメチレンテトラミンを酢酸に溶解させた溶液と、無水酢酸を原料とし、これをニトロ化したのち水を加えて加水分解し、ろ過して廃酸を分離したのち水洗し、ついで煮洗して得られた粗RDXを有機溶媒で溶解して晶出し、水洗後ろ過して再結晶することよりなるRDXの製造方法において、粗結晶及び若しくは再結晶されたRDXのうち、74〜125μm以下の粒子を除去することを特徴とするRDXの製造法。   A solution in which ammonium nitrate is dissolved in concentrated nitric acid, a solution in which hexamethylenetetramine is dissolved in acetic acid, and acetic anhydride as a raw material, which is nitrated, hydrolyzed with water, and filtered to separate waste acid Then, the crude RDX obtained by washing with water and then boiled is dissolved in an organic solvent to crystallize, washed with water, filtered and recrystallized. A method for producing RDX, wherein particles of 74 to 125 μm or less are removed from RDX. 除去される粒子は74μm以下であることを特徴とする請求項1記載のRDXの製造法。   The method for producing RDX according to claim 1, wherein the particles to be removed are 74 µm or less.
JP2012171562A 2012-08-02 2012-08-02 Manufacturing method of RDX Active JP5993241B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2012171562A JP5993241B2 (en) 2012-08-02 2012-08-02 Manufacturing method of RDX

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2012171562A JP5993241B2 (en) 2012-08-02 2012-08-02 Manufacturing method of RDX

Publications (2)

Publication Number Publication Date
JP2014031284A true JP2014031284A (en) 2014-02-20
JP5993241B2 JP5993241B2 (en) 2016-09-14

Family

ID=50281432

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012171562A Active JP5993241B2 (en) 2012-08-02 2012-08-02 Manufacturing method of RDX

Country Status (1)

Country Link
JP (1) JP5993241B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106554241A (en) * 2016-08-03 2017-04-05 湖北凯龙化工集团股份有限公司 High density bulking ammonium oil explosive-source explosive post production line and production method
KR20190073060A (en) * 2017-12-18 2019-06-26 주식회사 한화 Apparatus for rdx production and method for rdx production using the same
KR20190081347A (en) * 2017-12-29 2019-07-09 주식회사 한화 Manufaturing method for cyclotrimethylene trinitramine and cyclotrimethylene trinitramine manufactured by using thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5864297A (en) * 1981-10-09 1983-04-16 日産自動車株式会社 Composite propellant
JPS60226500A (en) * 1984-04-04 1985-11-11 アクチボラゲツト・ボツフオース Crystallization
JPH0316985A (en) * 1989-06-14 1991-01-24 Nissan Motor Co Ltd Solid propellant for rocket
JPH0333091A (en) * 1989-06-30 1991-02-13 Tech Res & Dev Inst Of Japan Def Agency Composition for explosive
JPH0648878A (en) * 1992-07-27 1994-02-22 Daicel Chem Ind Ltd Explosive composition
WO1997042137A1 (en) * 1996-05-06 1997-11-13 Eastman Chemical Company Explosive formulations
JP2009051692A (en) * 2007-08-27 2009-03-12 Nippon Koki Co Ltd Polyhedral rdx, method for making rdx polyhedral and method for producing spherical rdx

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5864297A (en) * 1981-10-09 1983-04-16 日産自動車株式会社 Composite propellant
JPS60226500A (en) * 1984-04-04 1985-11-11 アクチボラゲツト・ボツフオース Crystallization
JPH0316985A (en) * 1989-06-14 1991-01-24 Nissan Motor Co Ltd Solid propellant for rocket
JPH0333091A (en) * 1989-06-30 1991-02-13 Tech Res & Dev Inst Of Japan Def Agency Composition for explosive
JPH0648878A (en) * 1992-07-27 1994-02-22 Daicel Chem Ind Ltd Explosive composition
WO1997042137A1 (en) * 1996-05-06 1997-11-13 Eastman Chemical Company Explosive formulations
JP2009051692A (en) * 2007-08-27 2009-03-12 Nippon Koki Co Ltd Polyhedral rdx, method for making rdx polyhedral and method for producing spherical rdx

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JPN6016013572; 火薬ハンドブック , 1987, 51-53, 南條正男 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106554241A (en) * 2016-08-03 2017-04-05 湖北凯龙化工集团股份有限公司 High density bulking ammonium oil explosive-source explosive post production line and production method
KR20190073060A (en) * 2017-12-18 2019-06-26 주식회사 한화 Apparatus for rdx production and method for rdx production using the same
KR101996539B1 (en) 2017-12-18 2019-07-04 주식회사 한화 Apparatus for rdx production and method for rdx production using the same
KR20190081347A (en) * 2017-12-29 2019-07-09 주식회사 한화 Manufaturing method for cyclotrimethylene trinitramine and cyclotrimethylene trinitramine manufactured by using thereof
KR101999744B1 (en) * 2017-12-29 2019-07-12 주식회사 한화 Manufaturing method for cyclotrimethylene trinitramine and cyclotrimethylene trinitramine manufactured by using thereof

Also Published As

Publication number Publication date
JP5993241B2 (en) 2016-09-14

Similar Documents

Publication Publication Date Title
JP5993241B2 (en) Manufacturing method of RDX
CN108727334B (en) Production process of dabigatran etexilate mesylate
CN102320903A (en) Method for preparing high-quality energetic crystal material fine particles
US2362743A (en) Manufacture of dinitrotoluene
CN102863360A (en) Synthetic method of novel nitro arylideneamino guanidine derivatives
US2826611A (en) Process for making ar-dinitro-phenylureas
JP2009051692A (en) Polyhedral rdx, method for making rdx polyhedral and method for producing spherical rdx
KR101573616B1 (en) Process for Controlling Form and Particle Size by Recrystallization of N-Guanylurea-Dinitramide
KR20170036231A (en) Purifying method of dodecanedioic acid
CN110526877B (en) Synthetic method of 1-nitroso-3, 5, 7-trinitro-1, 3,5, 7-tetraazacyclooctane
CN111763154A (en) Method for synthesizing diethanol nitramine dinitrate
JP2010111665A (en) Method of producing 2-hydroxy-4-methylthiobutanoic acid
US2294592A (en) Preparation and purification of nitrated pentaerythritols
CN107540621B (en) Method for improving suction filtration efficiency of cyclotetramethylene tetranitramine synthetic product
US2481283A (en) Preparation of nitratoalkyl nitramines
US2370437A (en) Nitration process
CN105636933A (en) A method for preparing an intermediate of iopromide
US2858346A (en) Process of recrystallizing nitro explosives
Lee et al. Habit modification of 1, 1-diamino-2, 2-dinitroethylene (DADNE) by crystallization
US1691954A (en) Production of erythritol tetranitrate
JP2004196560A (en) Method for refining alkali iodide
US8466317B1 (en) Preparation of insensitive bis(2,2,-dinitropropyl) nitramine (BDNPN)
US1867962A (en) Manufacture of m-2-xylidine
US1503956A (en) Explosive and process of making same
KR101999744B1 (en) Manufaturing method for cyclotrimethylene trinitramine and cyclotrimethylene trinitramine manufactured by using thereof

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20150602

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20160316

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20160412

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20160517

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20160809

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20160819

R150 Certificate of patent or registration of utility model

Ref document number: 5993241

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250