Heavy metal ionic liquid chunk liquid film separating and recycling method

A technology of ionic liquid and recovery method, applied in chemical instruments and methods, improvement of process efficiency, water/sludge/sewage treatment, etc., can solve the problems of low mobility, difficult recycling of organic solvents, complicated operation, etc. Good separation effect, high separation efficiency, simple ingredients and simple operation

Inactive Publication Date: 2009-10-21
南通恒通机械制造有限公司
View PDF0 Cites 6 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a method for separation and recovery of heavy metal ionic liquid bulk liquid membrane, which solves the problems of complex operation, low mobility and difficult recycling of organic solvents in the prior art

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
  • Heavy metal ionic liquid chunk liquid film separating and recycling method
  • Heavy metal ionic liquid chunk liquid film separating and recycling method
  • Heavy metal ionic liquid chunk liquid film separating and recycling method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Embodiment 1: implement according to the following steps and relevant control parameters,

[0036] Step 1, select the ionic liquid [BMIM]PF with a purity of 98% 6 As a membrane solvent, P with a purity of 98% was chosen 507 As a carrier, the carrier and the ionic liquid are mixed according to a volume ratio of 0.5:99.5 to obtain a membrane solution, that is, a liquid membrane phase.

[0037] Step 2. Select 2.0mol / L HNO 3 as analytical phase 2;

[0038] Step 3, mix acetic acid and sodium acetate according to the volume ratio of 65:35 to obtain a buffer solution, and then mix the buffer solution with a concentration of 2.3×10 -3 mol / L PbSO to be recovered 4 The solution is mixed at a volume ratio of 90:10 to obtain material liquid phase 3;

[0039] Step 4. Add the liquid film phase 4 into the glass container 7, make the liquid surface overflow the edge of the lower opening of the glass tube 1, add the material liquid phase 3 into the glass container 7, and add the an...

Embodiment 2

[0041] Embodiment 2: choose the ionic liquid [BEIM]PF that purity is 98% 6 As a membrane solvent, P with a purity of 98% was chosen 507 As a carrier, the carrier and the ionic liquid are mixed according to the volume ratio of 0.3:99.7 to obtain the liquid film phase 4; 0.5mol / L HNO 3 As analytical phase 2; acetic acid and sodium acetate are mixed according to a volume ratio of 90:10 to obtain a buffer solution, and then the buffer solution is mixed with a concentration of 2.4×10 -3 mol / L of Cd(NO 3 ) 2 The solution is mixed according to the volume ratio of 88:12 to obtain the material liquid phase 3; the liquid film phase 4 is added to the glass container 7, the liquid level is overflowed over the lower opening edge of the glass tube 1, and the material liquid phase 3 is added to the glass container 7 At the same time, the analytical phase 2 is added to the glass tube 1, and the magnetic stirrer 6 is turned on to stir the liquid film phase 4 at a speed of 500 ± 50 rpm, so t...

Embodiment 3

[0042] Embodiment 3: choose the ionic liquid [BMIM]PF that purity is 98% 6 As a membrane solvent, P with a purity of 98% was chosen 507 As a carrier, the carrier and the ionic liquid are mixed according to the volume ratio of 1:99 to obtain the liquid film phase 4; 1.0mol / L H 2 SO 4 As analytical phase 2; acetic acid and sodium acetate are mixed according to a volume ratio of 15:85 to obtain a buffer solution, and then the buffer solution is mixed with a concentration of 2.5×10 -3 mol / L CuSO to be recovered 4 The solution is mixed according to the volume ratio of 93:7 to obtain the material liquid phase 3; the liquid film phase 4 is added to the glass container 7, so that the liquid level overflows the lower opening edge of the glass tube 1, and the material liquid phase 3 is added to the glass container 7 At the same time, add the analytical phase 2 into the glass tube 1, turn on the magnetic stirrer 6 to stir the liquid film phase 4 at a speed of 500±50 rpm, so that the h...

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

No PUM Login to View More

Abstract

The invention discloses a heavy metal ionic liquid chunk liquid film separating and recycling method. The method is implemented according to the following steps: using [BMIM]PF6 or [BEIM]PF6 as a film solvent and P507 as a carrier, mixing the ionic liquid and the carrier according to the volume ratio of 0.25-1.0:99.75-99.0 to obtain a liquid film phase; using HNO3 or H2SO4 as a resolution phase; mixing acetic acid and sodium acetate according to the volume ratio of 10-90:90-10 to obtain a buffer solution, and mixing the buffer solution with recycled heavy metallic salt solution according to the volume ratio of 95-85:5-15 to obtain a material liquid phase; adding the liquid film phase into a glass container, when the liquid level of the liquid film phase flows over the margin of the lower opening of a glass tube in the glass container, adding the material liquid phase into the glass container and simultaneously adding the resolution phase into the glass tube, starting a magnetic stirring apparatus to stir the liquid film phase, when the migration rate of the heavy metal ion liquid achieves over 95%, ending the stirring, and then transferring the liquid film phase and the resolution phase into a separatory funnel for layer separation to obtain the colorless aqueous phase solution of the lower layer as the transferred heavy metal ion liquid.

Description

Technical field: [0001] The invention belongs to the technical field of separation and recovery of heavy metals, and in particular relates to a method for separation and recovery of heavy metal ionic liquid bulk liquid membranes. Background technique: [0002] Since the beginning of the 21st century, worldwide environmental pollution has become increasingly serious. While modern industry provides a variety of materials such as dyes, medicines, fertilizers, cloth, and various performance materials for the development of human society, it also takes the earth we live on Get "disgraced", especially water pollution is particularly serious. As we all know, 70% of our earth is water, and water is the source of all things. Therefore, it is imminent to eradicate water pollution. Heavy metal pollution is one of the most harmful water pollution problems. Heavy metals refer to metals with a specific gravity greater than 5 (generally referring to metals with a density greater than 4....

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): C22B7/00C02F1/62C02F101/20
CPCY02P10/20
Inventor姚秉华裴亮钟晶晶王爽余晓皎
Owner南通恒通机械制造有限公司