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A waste flow type rainwater deep circulation purification device and its purification process

A recycling purification and rainwater technology, applied in runoff/rainwater treatment, combined device, filtration treatment, etc., can solve problems affecting the normal operation of sewage treatment plants, difficult renovation work, high treatment costs, etc., to achieve novel and reasonable structure, gas-liquid High isolation ability and high removal efficiency

Active Publication Date: 2020-09-08
XUZHOU UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] If according to the traditional method, the rainwater pipes containing the waste water are directly sent to the sewage pipe network and treatment system, on the one hand, the existing residential area is tight and the renovation work is difficult. After the renovation, if there is a large amount of rainwater, it will give urban sewage The treatment plant brings a large load impact, which affects the normal operation of the sewage treatment plant
[0009] Under the current technical conditions, the construction cost and operating cost of the equipment for treating impurities in rainwater will increase inevitably. The existing traditional process and treatment method have the disadvantages of long process flow, complicated control, large land occupation and high treatment cost.

Method used

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  • A waste flow type rainwater deep circulation purification device and its purification process
  • A waste flow type rainwater deep circulation purification device and its purification process
  • A waste flow type rainwater deep circulation purification device and its purification process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Manufacture the gas-liquid separation separator 2-9 of the present invention according to the following steps, and by weight fraction:

[0054] Step 1: Add 569 parts of ultrapure water with a conductivity of 0.69μS / cm into the reaction kettle, start the stirrer in the reaction kettle at a speed of 109rpm, start the heating pump, and raise the temperature in the reaction kettle to 79°C; add in sequence 79 parts of N-diisopropyl-2-chloroethylamine hydrochloride, bis[3-hydroxy-4-[(2-hydroxy-1-naphthyl)azo]-1-naphthalenesulfonate]chromic acid 99 parts of diethanolamine sodium salt, 169 parts of N,N'-diphenyl-N,N'-di(1-naphthyl)-1,5-naphthalenediamine, stirred until completely dissolved, and adjusted the pH value to 6.9, Adjust the speed of the agitator to 169rpm, the temperature is 109°C, and the esterification reaction takes 29 hours;

[0055] Step 2: Take 99 parts of 3,7-bis(1,1-dimethylethyl)-1-naphthalenesulfonate sodium and 89 parts of bis(β-chloroethyl)amine hydrochlor...

Embodiment 2

[0060] Manufacture the gas-liquid separation separator 2-9 of the present invention according to the following steps, and by weight fraction:

[0061] Step 1: Add 1519 parts of ultrapure water with a conductivity of 0.89μS / cm into the reactor, start the stirrer in the reactor at a speed of 269rpm, start the heating pump, and raise the temperature in the reactor to 99°C; add in order 169 parts of N-diisopropyl-2-chloroethylamine hydrochloride, bis[3-hydroxy-4-[(2-hydroxy-1-naphthyl)azo]-1-naphthalenesulfonato]chromic acid 169 parts of diethanolamine sodium salt, 359 parts of N,N'-diphenyl-N,N'-bis(1-naphthyl)-1,5-naphthalenediamine, stirred until completely dissolved, and adjusted the pH value to 8.9, Adjust the speed of the agitator to 269rpm, the temperature is 179°C, and the esterification reaction is 39 hours;

[0062] Step 2: Take 209 parts of 3,7-bis(1,1-dimethylethyl)-1-naphthalenesulfonate sodium and 169 parts of bis(β-chloroethyl)amine hydrochloride and grind them int...

Embodiment 3

[0067] Manufacture the gas-liquid separation separator 2-9 of the present invention according to the following steps, and by weight fraction:

[0068] Step 1: Add 919 parts of ultrapure water with a conductivity of 0.79μS / cm into the reactor, start the stirrer in the reactor at a speed of 169rpm, start the heat pump, and raise the temperature in the reactor to 89°C; add in sequence 119 parts of N-diisopropyl-2-chloroethylamine hydrochloride, bis[3-hydroxy-4-[(2-hydroxy-1-naphthyl)azo]-1-naphthalenesulfonate]chromic acid 149 parts of diethanolamine sodium salt, 259 parts of N,N'-diphenyl-N,N'-di(1-naphthyl)-1,5-naphthalenediamine, stirred until completely dissolved, and adjusted the pH value to 7.9, Adjust the speed of the agitator to 189rpm, the temperature is 129°C, and the esterification reaction is 32 hours;

[0069] Step 2: Take 159 parts of 3,7-bis(1,1-dimethylethyl)-1-naphthalenesulfonate sodium and 129 parts of bis(β-chloroethyl)amine hydrochloride and grind them into ...

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Abstract

The invention discloses a flow-discarding deep circulation purification device for rainwater and its purification process, which is composed of a fixed leg, a rainwater purification body chamber, an air intake pipe, an air outlet pipe, a circulation return pipe, a rainwater input system, a drainage pipe, and a control center. . The upper surface of the fixed leg is provided with a rainwater purification body warehouse, the air intake pipe and the air outlet pipe are arranged on the upper surface of the rainwater purification body warehouse and communicate with the interior of the rainwater purification body warehouse, and the air inlet pipe and the air outlet pipe The rainwater input system is located on one side of the fixed leg and communicates with the rainwater purification body compartment through the circulation return pipe. The number of the drainage pipes is 2 groups, and the drainage pipes are symmetrically arranged on the outer walls of both sides below the rainwater purification body compartment. The control center is located at the bottom of the fixed outriggers. The waste flow type rainwater deep circulation purification device described in the present invention has a novel and reasonable structure, is convenient to operate, has high efficiency in removing impurities in rainwater, and is suitable for purification treatment of different kinds of impurities in rainwater.

Description

technical field [0001] The invention belongs to the field of rainwater purification devices, and in particular relates to a flow-discarding deep circulation purification device for rainwater and a purification process thereof. Background technique [0002] With the increasing rate of urbanization and the hardening of roads, it is difficult for rainwater to infiltrate, resulting in frequent urban waterlogging. The government has proposed to vigorously build the concept of "sponge city" with natural accumulation, natural infiltration and natural purification. The Ministry of Housing and Urban-Rural Development issued the "Technical Guidelines for Sponge City Construction". Under the vigorous call of the country, the construction of sponge cities has gradually been recognized and familiarized by everyone. The construction of a sponge city is to reduce the runoff of rainwater and reduce the pressure of drainage pipes through "stagnation, storage and use", thereby reducing the p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/28C02F1/00B01D50/00
CPCC02F1/001C02F1/28C02F2103/001B01D50/20Y02W10/37
Inventor 王宏张林军张宝军刘晓玲
Owner XUZHOU UNIV OF TECH
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