Method for preparation of n-butyl nitrite

Patent metadata

Field	Value
Publication number	US-10125087-B2
Application number	US-201615747510-A
Country	US
Kind code	B2
Filing date	Sep 14, 2016
Priority date	Sep 16, 2015
Publication date	Nov 13, 2018
Grant date	Nov 13, 2018

Abstract

The invention discloses a method for the continuous preparation of n-butyl nitrite with a low content of n-butanol comprising the reaction of n-butanol, an acid and NaNO2 in a continuous way, in which the n-butanol, an acid and NaNO2 are mixed in a mixing device which provides for a pressure drop of at least 1 bar; the acid is selected from the group consisting of HCI, H2SO4, formic acid, methanesulfonic acid, and mixtures thereof; and the amount of HCI is at least 1.02 molar equivalent based on the molar amount of n-butanol.

First claim

The invention claimed is:

1. A method for the preparation of n-butyl nitrite;
wherein the method comprises a step STEP1, STEP1 comprises a reaction REAC1, and in REAC1 n butanol, an acid ACI and NaNO 2 are reacted;
REAC1 is done in a continuous way;
the n-butanol, ACI and NaNO 2 are mixed in a mixing device MIXDEV;
ACI is selected from the group consisting of HCl, H 2 SO 4 , formic acid, methanesulfonic acid, and mixtures thereof;
MIXDEV provides for a pressure drop DELTAP of at least 1 bar; and
the amount of ACI is at least 1.02 molar equivalent, the molar equivalent being based on the molar amount of n-butanol.

2. The method according to claim 1 , wherein MIXDEV is a static mixing device or a continuously working micro reactor.

3. The method according to claim 1 , wherein DELTAP is from 1 to 100 bar.

4. The method according to claim 1 , wherein the amount of ACI is from 1.02 to 1.5 molar equivalent.

5. The method according to claim 1 , wherein ACI is selected from the group consisting of HCl, H 2 SO 4 , formic acid, and mixtures thereof.

6. The method according to claim 1 , wherein the amount of NaNO 2 is from 1.0 to 3 molar equivalent, the molar equivalent being based on the molar amount of n-butanol.

7. The method according to claim 1 , wherein the reaction time of REAC1 is from 0.1 second to 2 hours.

8. The method according to claim 1 , wherein REAC1 is done in a loop shaped device LOOPDEV;
n-butanol, ACI and NaNO 2 are fed into LOOPDEV providing a reaction mixture REACMIX in LOOPDEV;
LOOPDEV comprises MIXDEV and a device CONVDEV for conveyance of REACMIX; and
the outlet of MIXDEV is connected to the inlet of CONVDEV and the outlet of CONVDEV is connected to the inlet of MIXDEV, thereby the loop is formed.

9. The method according to claim 8 , wherein CONVDEV is a pump.

10. The method according to claim 8 , wherein LOOPDEV comprises a device HEATDEV for heat exchange.

11. The method according to claim 8 , wherein LOOPDEV comprises a device GASSEPDEV gas separation.

12. The method according to claim 11 , wherein
the outlet of HEATDEV is connected to the inlet of MIXDEV,
the outlet of MIXDEV is connect to the inlet of GAS SEPDEV,
the outlet of GAS SEPDEV is connected to the inlet of CONVDEV, and
the outlet of CONVDEV is connected to the inlet of HEATDEV.

13. The method according to claim 12 , wherein n-butanol, ACI and NaNO 2 are fed into LOOPDEV between HEATDEV and MIXDEV.

14. The method according to claim 8 , wherein n-butanol, ACI and NaNO 2 are fed separately into LOOPDEV.

15. The method according to claim 8 , wherein the residence time RETI of REACMIX in LOOPDEV is from 0.1 second to 2 hours.

Assignees

• Lonza Ag

Inventors

• Taeschler Christoph
• Mayerhoeffer Ulrich
• Girard Christophe
• Bittel Michael
• Kalbermatten Rolf
• Arnold Claudio
• Garms Stefan
• Schnider Christian
• Tille Stefan
• Favre Manuel
• Raboud Guy
• Schnydrig Kilian
• Venetz Martin
• Eggel Thomas

Classifications

• B01J2219/00166

  controlling the residence time inside the reactor vessel · CPC title

• B01J19/1881

  externally, i.e. the mixture leaving the vessel and subsequently re-entering it · CPC title

• B01J2219/00162

  controlling the pressure · CPC title

• C07C201/04 Primary

  Preparation of esters of nitrous acid · CPC title

• B01J2219/00033

  Continuous processes · CPC title