Method and apparatus for producing nitrogen trifluoride

A technology of nitrogen trifluoride and ammonium bifluoride, which is applied in nitrogen trifluoride, chemical instruments and methods, ammonium fluoride, etc., can solve problems such as shaft seal failure, reliability problems, and high inverse mixing of reaction volume. To achieve the effect of avoiding corrosion problems

Inactive Publication Date: 2003-10-22
BOC GRP INC
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the high power input suggested in the Coronell patent generates high shear rates which will remove the passivation layer and expose the underlying turbine substrate to fluorine, thereby accelerating corrosion, especially at the tip of the mixing impeller
Corrosion therefore causes excessive vibration of the mixer shaft and premature failure of the mixer shaft seal
Even with very frequent maintenance in operation, essentially preventing vibration of the shaft, the combination of high-speed rotating seals and corrosive fluorine and hydrogen fluoride atmospheres will cause reliability problems
Additionally, the high mechanical energy input into the reactor via the flat-bladed turbine can lead to a high degree of back mixing of the reaction volume under substantially uniform operating conditions
In this case there is no opportunity to optimize the local reactor operating conditions

Method used

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  • Method and apparatus for producing nitrogen trifluoride
  • Method and apparatus for producing nitrogen trifluoride
  • Method and apparatus for producing nitrogen trifluoride

Examples

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Embodiment

[0064] This example uses something like image 3 reactor structure. NF 3 The reactor was constructed with a 4 meter long, 12 inch diameter schedule 40 monel tube with a flanged top and capped bottom. Spiral steam heating and water cooling coils are attached to the exterior of the reactor with a heat transfer cement. NF 3 Reactor baffles are in NF 3 Bottom of the reactor wall and NF 3 Coaxial 3.3 meter long schedule 10 Monel tubes with a 20 cm gap between the bottoms of the reactor baffle walls. The reactor was installed 0.5 m below the top flange for NH 4 F(HF) x By-product pressure riser (seal leg) overflow pipe. The gas distribution ring for stripping nitrogen is located in an annular gap 3 meters from the center of the top flange, at NF 3 Reactor Wall and NF 3 The reactor walls are approximately equally spaced. The main function of the nitrogen stripping gas is to establish a uniform temperature and suitable NH 4 F(HF) x cycle rate.

[0065] A pressure vessel ...

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Abstract

The invention provides a method and apparatus for producing nitrogen trifluoride. The invention involves passing a working fluid through a heat engine cycle and using the mechanical energy generated by the working fluid to produce sufficient mixing intensity within a nitrogen trifluoride reactor. The method utilizes a working fluid vapor jet, such as a hydrogen fluoride vapor jet, to impart sufficient energy to the mixing zone of a reactor in order to disperse gaseous fluorine within a liquid ammonium acid fluoride melt. A gaseous reaction product stream is removed from the reactor, the reaction product stream comprising nitrogen trifluoride and a working fluid vapor. The working fluid is then separated from the nitrogen trifluoride and recycled for reuse in the process, thereby completing a heat engine cycle.

Description

technical field [0001] The present invention relates to a method and device for producing nitrogen trifluoride from ammonia and elemental fluorine by utilizing ammonium bifluoride melt intermediate. Background technique [0002] Nitrogen trifluoride can be produced by the gas-phase reaction of ammonia and gaseous elemental fluorine. Reaction 1 illustrates the preparation of NF 3 desired gas-phase reaction. [0003] <chemistry num="001"> <chem file="03120687_cml001.xml" / > < / chemistry> (?H = -904 kJ / gmol NF 3 ) [0004] Response 1 [0005] where (g) represents the gas phase. Usually solid catalysts are used to lower the desired reaction temperature and increase NF 3 yield. However, due to the highly exothermic nature of Reaction 1, controlling the temperature of the reactor is very difficult. As a result, gas-phase ammonia and fluorine react to produce large amounts of HF, N 2 , N 2 F 2 and NH 4 F, while NF 3 T...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01F3/04B01F5/02B01F5/06B01J10/00B01J19/24C01B7/19C01B21/083C01C1/16
CPCB01F5/02B01J19/244C01B7/194C01C1/162B01F5/06B01F2215/0468B01J2219/00094B01J19/246B01F2215/0472B01J2219/00108B01F5/0659B01J2219/00006B01J10/002C01C1/16C01B21/0835B01F3/04099B01F23/23B01F25/20B01F25/40B01F25/435C01B21/083
Inventor D·P·小萨切尔V·R·莫汉
Owner BOC GRP INC
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