US20050188874A1 - Use of a microjet reactor for the production of initiating explosive - Google Patents
Use of a microjet reactor for the production of initiating explosive Download PDFInfo
- Publication number
- US20050188874A1 US20050188874A1 US10/901,973 US90197304A US2005188874A1 US 20050188874 A1 US20050188874 A1 US 20050188874A1 US 90197304 A US90197304 A US 90197304A US 2005188874 A1 US2005188874 A1 US 2005188874A1
- Authority
- US
- United States
- Prior art keywords
- reactor
- production
- initiating explosive
- use according
- explosive
- 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.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06C—DETONATING OR PRIMING DEVICES; FUSES; CHEMICAL LIGHTERS; PYROPHORIC COMPOSITIONS
- C06C7/00—Non-electric detonators; Blasting caps; Primers
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
- C06B21/0008—Compounding the ingredient
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
- C06B21/0033—Shaping the mixture
- C06B21/0066—Shaping the mixture by granulation, e.g. flaking
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B41/00—Compositions containing a nitrated metallo-organic compound
Definitions
- This invention relates to the use of a microjet reactor for the production of initiating explosive.
- initiating primers or initiating explosives with very small and reproducible crystal dimensions (typical sizes of ⁇ 30 ⁇ m) are needed so that good thermal coupling can be effected between the electrical heating resistances and the crystals. In other applications of initiating explosives it is also desirable that many small crystals be in contact with the igniting resistance in question.
- very small crystals for example in the range of 0.5 to 30 ⁇ m, preferably 1 to 20 ⁇ m, particularly preferably 1 to 10 ⁇ m
- microjet reactor for the production of initiating explosive, each of the starting solutions for explosive production in the microjet reactor being injected through a nozzle onto a common collision point into a reactor space enclosed by a reactor housing, a gas being admitted into the reactor space via an opening, and the resulting initiating explosive crystals being removed from the reactor housing together with the liquid and excess gas through a further opening.
- a microjet reactor is described, for example, in WO 00/61275, reference being expressly made here to the entire content of the disclosure of this publication.
- the initiating explosive can be won in a narrow, well-defined and adjustable grain-size spectrum.
- the size of the explosive crystals generated in precipitation can be reproducibly controlled by varying the operating parameters.
- the diameters of the reactant-supplying nozzles, the pump pressure, the temperatures and concentrations of the starting solutions, and the quantity of auxiliary gas can be varied.
- the nozzle diameter is preferably 10 to 1000 ⁇ m, particularly preferably 50 to 500 ⁇ m, and most particularly preferably 50 to 100 ⁇ m.
- the total throughput is preferably 10 to 1000 mL/minute, particularly preferably 50 to 500 mL/minute.
- the following initiating explosives can preferably be produced through the use according to the invention: potassium dinitrobenzofuroxanate, lead azide, lead picrate, lead trinitroresorcinate and cesium dinitrobenzofuroxanate.
- a further advantage of the use according to the invention is that fractional (and hazardous) screening can be omitted because of the well-defined crystal size of the initiating explosive.
- a sodium dibenzofuroxanate solution with a temperature of 23° C. and a concentration of 20 g/L and a potassium nitrate solution with a temperature of 23° C. and a concentration of 30 g/L were brought together with a nozzle pressure of 100 bar at each nozzle. Air was used as transporting gas. After two minutes' reaction, approximately 1 L of reaction liquid containing approximately 5 g of finely divided potassium dinitrobenzofuroxanate was obtained.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10334992.8 | 2003-07-31 | ||
DE10334992A DE10334992A1 (de) | 2003-07-31 | 2003-07-31 | Verwendung eines Mikrojetreaktors für die Herstellung von Initialsprengstoff |
Publications (1)
Publication Number | Publication Date |
---|---|
US20050188874A1 true US20050188874A1 (en) | 2005-09-01 |
Family
ID=33547045
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/901,973 Abandoned US20050188874A1 (en) | 2003-07-31 | 2004-07-30 | Use of a microjet reactor for the production of initiating explosive |
Country Status (3)
Country | Link |
---|---|
US (1) | US20050188874A1 (fr) |
EP (1) | EP1505047A3 (fr) |
DE (1) | DE10334992A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130008334A1 (en) * | 2010-03-16 | 2013-01-10 | Qinetiq Limited | Mems detonator |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108752150A (zh) * | 2018-07-09 | 2018-11-06 | 山西壶化集团股份有限公司 | 一种kbkg起爆药剂的制备方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2265230A (en) * | 1938-11-25 | 1941-12-09 | Western Cartridge Co | Basic lead styphnate and a process of making it |
US2395860A (en) * | 1943-11-05 | 1946-03-05 | American Cyanamid Co | Preparation of crystalline materials |
US20020119079A1 (en) * | 1999-12-10 | 2002-08-29 | Norbert Breuer | Chemical microreactor and microreactor made by process |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB741756A (en) * | 1953-02-24 | 1955-12-14 | Secr Defence Brit | Method for producing fine crystals of controlled particle size |
NL7709783A (nl) * | 1976-09-07 | 1978-03-09 | Imp Metal Ind Kynoch Ltd | Werkwijze voor het bereiden van springstof. |
US5156779A (en) * | 1989-04-27 | 1992-10-20 | E. I. Du Pont De Nemours And Company | Process and apparatus for producing ultrafine explosive particles |
DE3926466C2 (de) * | 1989-08-10 | 1996-12-19 | Christoph Dipl Ing Caesar | Mikroreaktor zur Durchführung chemischer Reaktionen von zwei chemischen Stoffen mit starker Wärmetönung |
JP3543347B2 (ja) * | 1994-01-24 | 2004-07-14 | 日本油脂株式会社 | 点火薬造粒物の製造方法 |
EP1165224B1 (fr) * | 1999-04-08 | 2002-09-18 | Bernd Penth | Procede et dispositif pour la realisation de processus chimiques et physiques |
US6454886B1 (en) * | 1999-11-23 | 2002-09-24 | Technanogy, Llc | Composition and method for preparing oxidizer matrix containing dispersed metal particles |
DE10049200A1 (de) * | 2000-10-05 | 2002-04-11 | Clariant Gmbh | Verfahren zur Herstellung von Azofarbmitteln |
-
2003
- 2003-07-31 DE DE10334992A patent/DE10334992A1/de not_active Withdrawn
-
2004
- 2004-07-28 EP EP04017847A patent/EP1505047A3/fr not_active Withdrawn
- 2004-07-30 US US10/901,973 patent/US20050188874A1/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2265230A (en) * | 1938-11-25 | 1941-12-09 | Western Cartridge Co | Basic lead styphnate and a process of making it |
US2395860A (en) * | 1943-11-05 | 1946-03-05 | American Cyanamid Co | Preparation of crystalline materials |
US20020119079A1 (en) * | 1999-12-10 | 2002-08-29 | Norbert Breuer | Chemical microreactor and microreactor made by process |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130008334A1 (en) * | 2010-03-16 | 2013-01-10 | Qinetiq Limited | Mems detonator |
Also Published As
Publication number | Publication date |
---|---|
EP1505047A2 (fr) | 2005-02-09 |
DE10334992A1 (de) | 2005-02-24 |
EP1505047A3 (fr) | 2006-11-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: DYNAMIT NOBEL AIS GMBH, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BREDE, UWE;BLEY, ULRICH;REEL/FRAME:015988/0259;SIGNING DATES FROM 20041021 TO 20041022 |
|
AS | Assignment |
Owner name: DELPHI TECHNOLOGIES, INC.,MICHIGAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:DYNAMIT NOBEL GMBH EXPLOSIVSTOFF UND SYSTEMTECHNIK;REEL/FRAME:017804/0818 Effective date: 20050914 Owner name: DELPHI TECHNOLOGIES, INC., MICHIGAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:DYNAMIT NOBEL GMBH EXPLOSIVSTOFF UND SYSTEMTECHNIK;REEL/FRAME:017804/0818 Effective date: 20050914 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |