Near-zero maintenance membrane-based integrated purification device for drinking water supply of villages and towns and a method for treating source water thereof

Patent metadata

Field	Value
Publication number	US-11827539-B2
Application number	US-202217955576-A
Country	US
Kind code	B2
Filing date	Sep 29, 2022
Priority date	Sep 29, 2021
Publication date	Nov 28, 2023
Grant date	Nov 28, 2023

Abstract

A near-zero maintenance integrated purification device for drinking water supply of villages and towns and a method for treating source water using this device are provided to solve the multi-pollution problems caused by microorganisms, turbidity, iron, manganese, taste and odor, and organic matter in the drinking water sources of villages and towns. The device includes a small-spacing folding plate speed sink regulating water tank, a small diameter tube reactor, a granular active carbon (GAC) slow-speed filter tank, a gravity-driven ultrafiltration membrane tank and an ipsilateral U-turn corridor clean water tank. The near-zero maintenance integrated purification device is applicable to different types of water sources (e.g., groundwater, lake water, reservoir water, spring water, snowmelt water, cellar water and rain water, etc.), and could efficiently remove kinds of pollutants, improving the biological and chemical safety of drinking water.

First claim

What is claimed is:

1. A near-zero maintenance integrated purification device for drinking water supply of villages and towns, comprising a folding plate speed sink regulating water tank, a tubular reactor, a granular active carbon (GAC) filter tank, a gravity-driven ultrafiltration membrane tank and an ipsilateral U-turn corridor clean water tank;
a first end of the folding plate speed sink regulating water tank is connected to raw water through a water inlet pipe, and a second end of the folding plate speed sink regulating water tank is connected to a water inlet of the tubular reactor through an outlet pipe; folded plates are installed in the folding plate speed sink regulating water tank to form vertical folding flows;
the tubular reactor comprises an inclined tube, a first perforated uniform water wall, a second perforated uniform water wall, and first perforated water collection pipes; the first perforated uniform water wall and the second perforated uniform water wall are set orderly at an inlet area of the tubular reactor; the first perforated uniform water wall and the second perforated uniform water wall are located at a lower part of an ineffective area of the inclined tube; holes of the first perforated uniform water wall and the second perforated uniform water wall are interlaced; an upper part of the inclined tube is a clean water collection area, and a lower part of the inclined tube is a water distribution area; the first perforated water collection pipes are installed in the clean water collection area;
a water collection channel is arranged between the tubular reactor and the GAC filter tank; the GAC filter tank comprises a first main aeration pipe, first aeration branch pipes, water distribution holes, a support layer, an activated carbon layer and a second perforated water collection pipe; the first main aeration pipe, the water distribution holes, the support layer, the activated carbon layer and the second perforated water collection pipe of the GAC filter tank are arranged orderly in the GAC filter tank from bottom to top; the first aeration branch pipes are connected to the first main aeration pipe, and the water collection channel connected to the GAC filter tank through the water distribution holes;
the GAC filter tank is connected to the gravity-driven ultrafiltration membrane tank through the second perforated water collection pipe; in the gravity-driven ultrafiltration membrane tank, a second main aeration pipe, a membrane module, and a water collection pipe are arranged orderly from bottom to top; second aeration branch pipes of the gravity-driven ultrafiltration membrane tank are connected to the second main aeration pipe;
the gravity-driven ultrafiltration membrane tank connected to the ipsilateral U-turn corridor clean water tank through the water collection pipe; partition walls are arranged in the ipsilateral U-turn corridor clean water tank to form a push flow pattern; and a suction well connected to a rotary corridor is provided at a bottom of the ipsilateral U-turn corridor clean water tank.

2. The near-zero maintenance integrated purification device according to claim 1 , wherein the water inlet pipe is equipped with a water inlet pump and a water inlet valve; a distance between adjacent two folded plates is 0.2-1.0 m; a distance between the first perforated uniform water wall and the second perforated uniform water wall is 0.5-1.5 m, and a distance between two adjacent first perforated water collection pipes is 0.2-0.4 m.

3. The near-zero maintenance integrated purification device according to claim 1 , wherein the gravity-driven ultrafiltration membrane tank is equipped with a dissolved oxygen detector; and the membrane module is a water grass type membrane module, a column type membrane module or a curtain type membrane module.

4. The near-zero maintenance integrated purification device according to claim 1 , wherein a circulation pipe is provided between the water collection channel and the gravity-driven ultrafiltration membrane tank, and a circulation valve and a circulation pump are set on the circulation pipe.

5. The near-zero maintenance integrated purification device according to claim 1 , wherein a bypass pipe line is arranged between the gravity-driven ultrafiltration membrane tank and the water collection channel, and the bypass pipe line is controlled by a crossing valve.

6. The near-zero maintenance integrated purification device according to claim 1 , Wherein the GAC filter tank is equipped with an energy-saving double aeration device and a double-layer steel cross-hole block, and the energy-saving double aeration device is one of a microporous aeration disc, a titanium plate, a micro-nano aeration air pipe, and a perforated aeration air pipe.

7. The near-zero maintenance integrated purification device according to claim 1 , wherein the ipsilateral U-turn corridor clean water tank is equipped with disinfection facilities; the disinfection facilities are connected to the ipsilateral U-turn corridor clean water tank through a chemical inlet pipe; and the chemical inlet pipe is equipped with a metering pump.

8. The near-zero maintenance integrated purification device according to claim 1 , wherein dredge buckets are installed at a bottom of the folding plate speed sink regulating water tank; a sediment sludge is discharged via a first perforated mud discharge pipe, and the first perforated mud discharge pipe is controlled by a first mud valve; a regulating water tank outlet valve is arranged on the outlet pipe of the folding plate speed sink regulating water tank; the suction well is connected to an outlet water pipe, and the outlet water pipe is equipped with a water valve and a pressure pump; the bottom of the ipsilateral U-turn corridor clean water tank is provided with a discharge valve; a second perforated mud discharge pipe is set at a bottom of the tubular reactor, and the second perforated mud discharge pipe is controlled by a second mud valves; a third perforated mud discharge pipe is set at a bottom of the GAC filter tank, and the third perforated mud discharge pipe is controlled by a third mud valve; a fourth perforated mud discharge pipe is set at a bottom of the gravity-driven ultrafiltration membrane tank, and the fourth perforated mud discharge pipe is controlled by a fourth mud valve.

9. The near-zero maintenance integrated purification device according to claim 4 , wherein the circulation pump, a metering pump and an energy-saving double aeration device are connected to a solar photovoltaic panel and are powered by the solar photovoltaic panel.

10. A method of treating source water using the near-zero maintenance integrated purification device according to claim 1 , wherein the method comprises the following steps:
step 1) the raw water flows into the folding plate speed sink water regulating tank; sand and large particles decrease in a process of flowing up and down, sink to a bottom of the folding plate speed sink regulating water tank, and are discharged through a first perforated mud discharge pipe;
step 2) after initial sedimentation of the folding plate speed sink regulating water tank, the raw water flows into the tubular reactor and enters the water distribution area through the first perforated uniform wall and the second perforated uniform wall orderly; when the raw water flows through the inclined tube, the larger particles and suspended matter sink to a bottom of the tubular reactor and are discharged through a second perforated mud discharge pipe; the raw water flows into the water collection channel through the first perforated water collection pipe in the clean water collection area to obtain precipitated water;
step 3) after precipitation, the precip

Assignees

• Harbin Inst Technology

Inventors

• Liang Heng
• Tang Xiaobin
• Guo Xishou
• Wang Jinlong
• Gong Weijia

Classifications

• C02F1/444 Primary

  by ultrafiltration or microfiltration · CPC title

• B01D61/146

  comprising multiple ultrafiltration steps · CPC title

• B01D61/18

  Apparatus therefor · CPC title

• C02F9/00 Primary

  Multistage treatment of water, waste water or sewage · CPC title

• C02F1/001

  Processes for the treatment of water whereby the filtration technique is of importance (C02F1/44 takes precedence; construction of filters in general B01D24/00 - B01D41/00) · CPC title