Method for producing ultra-pure yellow phosphorus

A production method, yellow phosphorus technology, applied in chemical instruments and methods, phosphorus compounds, inorganic chemistry, etc., can solve the problems of low removal rate, explosion, and increased purification cost, and achieve easy industrial production and save the recovery system , the effect of reducing investment

Active Publication Date: 2008-07-09
SICHUAN UNIV +1
View PDF2 Cites 19 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

As can be seen from the above steps, the mechanical impurities in industrial yellow phosphorus are removed by distillation (physical method), and the most important impurities arsenic and organic matter in industrial yellow phosphorus are removed by chemical methods. The existing shortcomings mainly include: (1) Use concentrated sulfuric acid to stir and react with industrial yellow phosphorus, then stir and react industrial yellow phosphorus with nitric acid and oxidation enhancer
The safety of the stirring reaction between concentrated sulfuric acid and industrial yellow phosphorus is extremely low. There have been reports at home and abroad that this method has caused explosions; when the treated yellow phosphorus is mixed with nitric acid and oxidation enhancer, many data have proved that the effect of removing arsenic is limited. (See "Preliminary Study on the Production Process of High-purity Yellow Phosphorus", Yang Luhua, Ma Xinliang, Inorganic Salt Industry, Volume 36, No. 2, 2004; "Experimental Research on Removing Arsenic from Yellow Phosphorus by Aqueous Phase Oxidation", Ren Y...

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for producing ultra-pure yellow phosphorus
  • Method for producing ultra-pure yellow phosphorus
  • Method for producing ultra-pure yellow phosphorus

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] The process flow of this embodiment is shown in Figure 1, and the process steps are extraction, zone melting, and vacuum microfiltration in sequence.

[0046] 1. Extraction

[0047] The extractant is di(2-ethylhexyl)phosphoric acid, and the diluent is kerosene. In the organic phase, the volume percentage of the extractant is 15%, and the volume percentage of the diluent is 85%. The volume ratio of the organic phase to the industrial yellow phosphorus is 1:3.

[0048] The extraction reactor is an ordinary glass jacketed reactor, in which hot water circulates at 70°C, then the organic phase is added, and nitrogen is introduced into the reactor. When the air in the reactor is completely exhausted, the industrial yellow phosphorus The phosphorus is pressed into the reactor from the phosphorus pressing tank, and the extraction is carried out under the protection of nitrogen, the stirring line speed is 200r / min, and the stirring time is 45min. After stopping the stirring, d...

Embodiment 2

[0075] The process flow of this embodiment is shown in Figure 1, and the process steps are extraction, zone melting, and vacuum microfiltration in sequence.

[0076] 1. Extraction

[0077] The extractant is tributyl phosphate, and the diluent is paraffin oil. In the organic phase, the volume percentage of the extractant is 30%, and the volume percentage of the diluent is 70%. The volume ratio of the organic phase to the industrial yellow phosphorus is 1:3.

[0078] The extraction reactor is an ordinary glass jacketed reactor, in which hot water circulates at 70°C, then the organic phase is added, and nitrogen is introduced into the reactor. When the air in the reactor is completely exhausted, the industrial yellow phosphorus Press it into the reactor from the phosphorus pressing tank, and extract it under the protection of nitrogen. The stirring line speed is 600r / min, and the stirring time is 35min. After stopping the stirring, discharge the organic phase, wash the yellow p...

Embodiment 3

[0093] The process flow of this embodiment is shown in Figure 1, and the process steps are extraction, zone melting, and vacuum microfiltration in sequence.

[0094] 1. Extraction

[0095] Extractant is two (2-ethylhexyl) phosphoric acid and tributyl phosphate, the volume ratio of two (2-ethylhexyl) phosphoric acid and tributyl phosphate is 1: 1, diluent is paraffin oil, in organic phase, The volume percentage of the extractant is 20%, and the volume percentage of the diluent is 80%. The volume ratio of the organic phase to the industrial yellow phosphorus is 1:2.

[0096] The extraction reactor is an ordinary glass jacketed reactor, in which hot water circulates at 70°C, then the organic phase is added, and nitrogen is introduced into the reactor. When the air in the reactor is completely exhausted, the industrial yellow phosphorus Press it into the reactor from the phosphorus pressing tank, and extract it under the protection of nitrogen, the stirring line speed is 800r / mi...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
Apertureaaaaaaaaaa
Login to view more

Abstract

Disclosed is a production method of ultra-pure yellow phosphorus, which uses the material of industrial yellow phosphorus, and the industrial yellow phosphorus is prepared to be the ultra-pure yellow phosphorus via extracting, zone melting, pressurizing or depressurizing micro-filtration sequentially. Extracting agent is at least one of di-(2-ethylhexyl) phosphoric acid, tributyl phosphate or calixarene, diluting agent is kerosene or paraffin oil or chloroform or carbon tetrachloride, and extraction technological parameter is that the volume ratio of organic phase and the industrial yellow phosphorus is 1:2-1:3. Apparatus for zone melting comprises a zone molten pool, a ring heater, an annular chiller and a driving device, wherein the ring heater and the annular chiller are assembled around the zone molten pool, and are arranged at intervals along the axial direction of the zone molten pool, the pressurizing or depressurizing micro-filtration utilizes a pressurizing or depressurizing filter with grade of 0.1 um-0.5 um. Utilizing the invention of the method to purify the industrial yellow phosphorus, the purity of yellow phosphorus products can reach 99.99%-99.9999%, and the yield coefficient can reach 73.2%-88.4%.

Description

technical field [0001] The invention belongs to a production method of ultra-pure yellow phosphorus, in particular to a method for producing ultra-pure yellow phosphorus by using industrial yellow phosphorus as a raw material. Background technique [0002] Industrial yellow phosphorus is made of phosphate rock in an electric furnace with SiO 2 It is obtained by high-temperature reduction reaction with coke, the purity is generally about 99.8%, and contains the following impurities: [0003] Metal elements: Ca, Fe, Al, Mg, Sr, Mn, Na, K, Ti, V, Cr, Ni, Ga, Cd, Cu, Sb, Pb, Zn, Sn, U. [0004] Semi-metal elements: Se, Si, C, B, As, Bi. [0005] Organic matter: more than 30 kinds of phenol, anthracene, tar and polyatomic polycyclic aromatic hydrocarbons. The color of yellow phosphorus is related to organic impurities, especially perylene and anthanthrene. About 70% of the total organic impurities in yellow phosphorus are the following substances: carbazole, pyrene, anthracen...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C01B25/047
Inventor 李军任永胜金央罗建洪段潇潇
Owner SICHUAN UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products