PE20091146A1 - IMPROVED PROCEDURE FOR PREPARING HYDROCIANIC ACID - Google Patents
IMPROVED PROCEDURE FOR PREPARING HYDROCIANIC ACIDInfo
- Publication number
- PE20091146A1 PE20091146A1 PE2008001847A PE2008001847A PE20091146A1 PE 20091146 A1 PE20091146 A1 PE 20091146A1 PE 2008001847 A PE2008001847 A PE 2008001847A PE 2008001847 A PE2008001847 A PE 2008001847A PE 20091146 A1 PE20091146 A1 PE 20091146A1
- Authority
- PE
- Peru
- Prior art keywords
- gas
- reactor
- gaseous
- formamide
- hydrocianic
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 5
- 239000002253 acid Substances 0.000 title 1
- 239000007789 gas Substances 0.000 abstract 5
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 abstract 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 2
- ZHNUHDYFZUAESO-NJFSPNSNSA-N aminoformaldehyde Chemical compound N[14CH]=O ZHNUHDYFZUAESO-NJFSPNSNSA-N 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 230000018044 dehydration Effects 0.000 abstract 1
- 238000006297 dehydration reaction Methods 0.000 abstract 1
- 239000003345 natural gas Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C3/00—Cyanogen; Compounds thereof
- C01C3/02—Preparation, separation or purification of hydrogen cyanide
- C01C3/0204—Preparation, separation or purification of hydrogen cyanide from formamide or from ammonium formate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0093—Microreactors, e.g. miniaturised or microfabricated reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00783—Laminate assemblies, i.e. the reactor comprising a stack of plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00819—Materials of construction
- B01J2219/00822—Metal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00819—Materials of construction
- B01J2219/00835—Comprising catalytically active material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00781—Aspects relating to microreactors
- B01J2219/00873—Heat exchange
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
EL CUAL COMPRENDE LA DESHIDRATACION CATALITICA DE FORMAMIDA GASEOSA EN UN REACTOR TUBULAR, EN EL QUE LA FORMAMIDA GASEOSA, QUE HA SIDO CALENTADA A TEMPERATURAS QUE VAN DE 330ºC A 400 ºC, ES CONDUCIDAAL REACTOR TUBULAR PARA FORMAR UN GAS DE PROCESO QUE CONTIENE ACIDO CIANHIDRICO GASEOSO, AGUA Y FORMAMIDA QUE NO HA REACCIONADO, EN EL QUE LA TEMPERATURA DEL GAS DE PROCESO AUMENTA A LO LARGO DEL REACTOR TUBULAR EN 0,25 HASTA 0,75 K/cm. EL PROCEDIMIENTO SE LLEVA A CABO TENIENDO EL GAS EN EL REACTOR UNA TEMPERATURA QUE VA DE 330 ºC A 600 ºC; DONDE EL REACTOR ES CALENTADO MEDIANTE EL GAS DE ESCAPE CALIENTE PROCEDENTE DE UN QUEMADOR DE GAS NATURAL Y CONDUCIDO EN LA MISMA CORRIENTE QUE EL GAS DE PROCESO. ADEMAS, EL PROCEDIMIENTO SE LLEVA A CABO A UNA PRESION QUE VA DE 70 A 350 mbar EN UN REACTOR MULTITUBULARWHICH INCLUDES THE CATALYTIC DEHYDRATION OF GASEOUS FORMAMIDE IN A TUBULAR REACTOR, IN WHICH THE GASEOUS FORMAMIDE, WHICH HAS BEEN HEATED TO TEMPERATURES VARING FROM 330ºC TO 400ºC, IS CONDUCTED TO THE TUBULAR REACTOR TO FORM A GASEOUS GAS TO FORM A GAS OF GASEOUS CIENOS , WATER AND FORMAMIDE THAT HAS NOT REACTED, IN WHICH THE TEMPERATURE OF THE PROCESS GAS INCREASES THROUGHOUT THE TUBULAR REACTOR BY 0.25 TO 0.75 K / cm. THE PROCEDURE IS CARRIED OUT HAVING THE GAS IN THE REACTOR A TEMPERATURE RANKING FROM 330 ºC TO 600 ºC; WHERE THE REACTOR IS HEATED USING THE HOT EXHAUST GAS FROM A NATURAL GAS BURNER AND CONDUCTED IN THE SAME CURRENT AS THE PROCESS GAS. ALSO, THE PROCEDURE IS CARRIED OUT AT A PRESSURE VARING FROM 70 TO 350 mbar IN A MULTITUBULAR REACTOR
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP07119521 | 2007-10-29 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PE20091146A1 true PE20091146A1 (en) | 2009-09-03 |
Family
ID=40328449
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PE2008001847A PE20091146A1 (en) | 2007-10-29 | 2008-10-29 | IMPROVED PROCEDURE FOR PREPARING HYDROCIANIC ACID |
Country Status (3)
| Country | Link |
|---|---|
| AR (1) | AR072760A1 (en) |
| PE (1) | PE20091146A1 (en) |
| WO (1) | WO2009056470A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016508481A (en) * | 2013-03-01 | 2016-03-22 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | Method for the synthesis of hydrocyanic acid from a back reactor packed with formamide |
| AT515109B1 (en) * | 2013-12-16 | 2015-06-15 | Bertrams Chemieanlagen Ag | Falling film evaporator |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1024070B (en) * | 1956-04-12 | 1958-02-13 | Degussa | Continuous production of hydrocyanic acid |
| DE3525749A1 (en) * | 1985-07-19 | 1987-01-29 | Basf Ag | METHOD FOR CLEAVING FORMAMIDE TO BLUE ACID AND WATER |
| DE10138553A1 (en) * | 2001-08-06 | 2003-05-28 | Basf Ag | Hydrogen cyanide production by dehydration of gaseous formamide containing atmospheric oxygen, uses a catalyst containing metallic iron or iron oxide, especially in the form of Raschig rings or a static packing mixer |
| DE10256578A1 (en) * | 2002-12-04 | 2004-06-17 | Basf Ag | Hydrogen cyanide from formamide |
-
2008
- 2008-10-21 WO PCT/EP2008/064171 patent/WO2009056470A1/en not_active Ceased
- 2008-10-28 AR ARP080104711A patent/AR072760A1/en active IP Right Grant
- 2008-10-29 PE PE2008001847A patent/PE20091146A1/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| AR072760A1 (en) | 2010-09-22 |
| WO2009056470A1 (en) | 2009-05-07 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FA | Abandonment or withdrawal |