Unlock instant, AI-driven research and patent intelligence for your innovation.

Preparation method of low-chlorine chemical engineering discharged water recycling circulating water

A technology for chlorination and circulating water, applied in chemical instruments and methods, multi-stage water/sewage treatment, neutralized water/sewage treatment, etc. pH value increase and other problems, to achieve the effect of small total time consumption, simple operation, continuous process operation

Inactive Publication Date: 2021-10-19
兰州石化职业技术大学
View PDF16 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In view of this, the present invention provides a method for the preparation of low-chlorinated industrial waste water recycling circulating water, which solves the problem that the existing chemical precipitation method for chlorine removal is likely to cause secondary pollution and cannot meet the requirements for chemical waste water treatment. Technical problems, but also solve the problem of the pH value of the solution caused by the ultra-high calcium aluminum precipitation method

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
  • Preparation method of low-chlorine chemical engineering discharged water recycling circulating water
  • Preparation method of low-chlorine chemical engineering discharged water recycling circulating water
  • Preparation method of low-chlorine chemical engineering discharged water recycling circulating water

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] The technical process of this embodiment please refer to the appendix figure 1, Measure 100ml of chemical waste water into the reactor, slowly raise the temperature to 25°C; add 0.4g of calcium oxide slurry into the reactor, and react at a constant temperature at 280rpm / min for 25min to form a primary solution; the primary solution is vacuum filtered to form The lower clarified liquid is directly introduced into the reactor, and the upper sediment is collected and dried for use; the porous microspheres containing 0.4g calcium hydroxide and 0.33g sodium metaaluminate are added to the reactor, and the reaction is performed at a constant temperature at a speed of 430rpm / min. After 40 minutes, slowly add 0.7g of calcium bicarbonate, react at a constant temperature for 20 minutes, filter the formed solution again, collect the obtained secondary clarified liquid in a clean container, and recover the formed precipitate for reuse. The test results of the secondary clarification...

Embodiment 2

[0038] Measure 100ml of chemical waste water into the reactor, and slowly raise the temperature to 25°C; add 0.4g of 0.5 calcium hydroxide slurry into the reactor, and react at a constant temperature of 280rpm / min for 25min to form a primary solution; the primary solution is vacuum filtered , the formed lower clarified liquid is directly introduced into the reactor, and the upper precipitate is collected and dried for later use; the porous microspheres containing 0.4g calcium hydroxide and 0.33g sodium metaaluminate are added to the reactor, and at a speed of 430rpm / min React at a constant temperature for 40 minutes, slowly add 0.7g of calcium bicarbonate, react at a constant temperature for 20 minutes, filter the formed solution again, collect the obtained secondary clarified liquid in a clean container, and recover the formed precipitate for reuse. The test results of the secondary clarification liquid are shown in Table 1.

Embodiment 3

[0040] Measure 100ml of chemical waste water into the reactor, and slowly raise the temperature to 25°C; add 0.4g of calcium oxide slurry into the reactor, and react at a constant temperature of 280rpm / min for 25min to form a primary solution; the primary solution is vacuum filtered to form The lower layer of clear liquid is directly introduced into the reactor, and the upper layer of sediment is collected and dried for use; 0.5g of calcium hydroxide and 0.44g of sodium metaaluminate are mixed evenly and then added to the reactor, and reacted at a constant temperature of 430rpm / min for 40min, slowly Add 0.7g of calcium bicarbonate, react at constant temperature for 20 minutes, filter the formed solution again, collect the obtained secondary clarified liquid in a clean container, and recover the formed precipitate for reuse. The test results of the secondary clarification liquid are shown in Table 1.

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 preparation method of low-chlorine chemical engineering discharged water recycling circulating water, and relates to the field of removal of chloride ions and recycling of circulating water. The method comprises the following steps: reacting precipitant slurry with discharged water, preferably removing SO4<2-> and CO3<2-> ions in water, conducting filtering to form a clear liquid, adding an ultrahigh calcium-aluminum precipitation mixture into the clear liquid according to a certain ratio to remove chloride ions, slowly adding a pH value regulator after the reaction time is ended, reducing the pH value of the solution to 6.8-8.5, and conducting filtering to form secondary clarified liquid meeting the index requirements of the circulating water. A by-product Fremy's salt precipitate formed in the process can be used as an adsorbent for heavy metal ions in sewage after being treated. The method is simple to operate, rapid and efficient, the total consumed time is less than 1.5 h, continuous process operation can be realized, zero pollution and zero emission are basically realized, and the method has industrial prospects.

Description

technical field [0001] The invention relates to the field of chloride ion removal and recycling of circulating water, in particular to a preparation method for recycling recycled water from low-chlorinated industrial waste water. Background technique [0002] Cooling circulating water accounts for more than 90% of the total industrial water consumption. It is required that the pH value of the solution is 6.8-8.5, the conductivity is 800-1500μs / cm, and the chloride ion concentration is lower than 200mg / l. At present, the concentration of chloride ions in chemical industry wastewater is generally 480-550mg / l, which is already relatively low compared to high-salt wastewater. Negative Effects. In order to meet the requirements for the use of circulating water, combined with the low concentration of chloride ions in chemical industry wastewater, currently feasible methods for removing chloride ions in chemical industry wastewater mainly include ion exchange, evaporation, membran...

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
Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/00C02F101/10C02F101/12
CPCC02F9/00C02F2101/101C02F1/001C02F1/66C02F2101/12C02F2101/10
Inventor 王海孙耀华谢恒卢勇王刚任张真张新发徐成王继元刘珂侯侠
Owner 兰州石化职业技术大学