Method for removing As (III) in wastewater through enhanced coagulation

A waste water and coagulation technology, applied in the field of water treatment, can solve problems such as low efficiency, high cost, and increased oxidant input, and achieve the effects of improving the pH environment, saving costs, and improving coagulation efficiency

Active Publication Date: 2020-06-30
NANJING AGRICULTURAL UNIVERSITY
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technical means described in the current methods involve combining two steps together - first performing both primary and secondary processes before reactivating the main function of Ascothiacal Acerbium Oxoferrite Colloidal Particles (CASNOPO3/A2 O4)). By controllably increasing or decreasing the concentration ratio between Ca1/Ca, allowing for continuous oxalysis without stopping downstream reactions. Additionally, the use of specific types of metal salts allows for precise control over the formation of CoAs and PbS nanoparcles while maintaining good collagen structure. Overall, these techniques enhance the performance and economics of the existing treatments for heavy metals contamination in industrial waters such as coal mineral flue gas desulfurizers.

Problems solved by technology

Technological Problem addressed in this patents relates to finding ways to enhance the effectiveness of reducing arsenicity caused from drinking sources like sorghum juice without causing harmful effects upon human health. Current techniques involve either chemical reactions involving different metals or complex processes requiring expensive materials.

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 removing As (III) in wastewater through enhanced coagulation
  • Method for removing As (III) in wastewater through enhanced coagulation
  • Method for removing As (III) in wastewater through enhanced coagulation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Step 1), add to the water samples with the As(III) content of 1.0mg / L whose initial pH values ​​are pH=4, pH=5, pH=6, pH=7, pH=8, and pH=9 respectively. 15mg / L of CaO 2 , continue stirring for 5min at a speed of 200rpm; after the end, measure the CaO 2 For the oxidation rate of As(III), after testing, when the initial pH values ​​are pH=4, pH=5, pH=6, pH=7, pH=8, pH=9, CaO 2 The oxidation rates to As(III) were 32%, 34%, 51%, 63%, 72% and 85%, respectively. i.e. in step 1) CaO 2 A pre-oxidation effect (incomplete oxidation) occurs on As(III).

[0045] Step 2), adding 50mg / L of titanium sulfate to the water sample after the treatment in the above step 1) respectively, stirring at a speed of 200rpm for 5min, adjusting the speed to 40rpm, stirring continuously for 10min, and measuring the supernatant after standing for 20min. The residual arsenic concentration in the solution.

[0046] At the same time, a comparison experiment of direct coagulation was set up for th

Embodiment 2

[0048] Step 1), add 20mg / L CaO to the water sample (pH=5.0) containing As(III) 2 , continue stirring for 2.5min at a speed of 250rpm;

[0049] Step 2), add 80mg / L of titanium sulfate coagulant to the above water sample, stir at 400rpm for 3min, adjust the speed to 60rpm, continue stirring for 20min, and measure the remaining arsenic in the supernatant after standing for 30min. concentration.

[0050] According to the above experimental steps, five groups of parallel experiments with initial As(III) concentrations of 0.1, 0.2, 0.5, 0.8 and 1.0 mg / L were set respectively, and CaO in each group was determined after step 1). 2 Oxidation rate of As(III); the results are: CaO 2 The oxidation rates of As(III) were 81%, 82%, 62%, 42% and 35%, respectively.

[0051] At the same time, a comparison experiment of direct coagulation was set up for five groups of parallel experiments, that is, only the coagulation experiment of step 2) was performed under the same conditions, and CaO

Embodiment 3

[0053] Step 1), add 100mg / L CaO to the water sample (pH 7.0) with As(III) content of 1.0mg / L 2 , continue stirring for 2min at a rotating speed of 500rpm, after step 1), measure the CaO 2 The oxidation rate to As(III) was 82%.

[0054] Step 2), adding titanium tetrachloride coagulant to the above water sample, stirring at 500rpm for 3min, adjusting the speed to 80rpm, stirring continuously for 30min, and measuring the residual arsenic concentration in the supernatant after standing for 40min.

[0055] Aiming at the above steps, five groups of parallel experiments were set up with the dosage of titanium tetrachloride being 50, 100, 200, 300, 400, and 500 mg / L, respectively. The coagulation experiment of step 2). Under the same conditions, compare CaO 2 The removal efficiency of As in the pre-oxidation enhanced coagulation and the direct coagulation process is compared, and the comparison results are as follows image 3 The results show that even if the dosage of coagulan

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 belongs to the field of wastewater treatment, and discloses a method for removing As (III) in wastewater by enhanced coagulation, which mainly comprises the following steps: (1) adding acertain amount of calcium peroxide into As (III) containing wastewater, and stirring; and (2) adding an inorganic coagulant to carry out coagulation treatment. According to the method, in the treatment process, on one hand, calcium peroxide plays a role of an oxidizing agent; As (III) is converted into As (V), and on the other hand, the pH environment in the water body solution is improved by utilizing slow hydrolysis of calcium peroxide in the water body solution, so that the pH in the coagulating sedimentation process is maintained at a slightly alkaline level beneficial to coagulating sedimentation, the coagulating efficiency is improved, and meanwhile, the efficient coagulating efficiency and oxidation efficiency are realized. The method is simple to operate and low in cost, does notneed additional equipment investment, and can be widely applied to advanced treatment of arsenic-containing industrial wastewater and treatment of arsenic-polluted underground water or drinking water.

Description

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

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
Owner NANJING AGRICULTURAL UNIVERSITY
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