US-12623926-B2 - Bidirectional flow pulse-based water body phosphorus removal apparatus and method, and organic nutrient soil

US12623926B2US 12623926 B2US12623926 B2US 12623926B2US-12623926-B2

Abstract

A bidirectional flow pulse-based water body phosphorus removal apparatus and a method, and an organic nutrient soil. The water body phosphorus removal apparatus includes: a prefiltration unit, a bidirectional flow phosphorus removal filtration pool, a bidirectional water collection and distribution system, a filtration pool stratified gas pulse system, a water production tank and a control system. A filtration layer filled with a phosphorus removal filtration material is provided in the bidirectional flow phosphorus removal filtration pool. The control system is used for controlling the bidirectional water collection and distribution system to alternately perform upward water in-and-out flow and downward water in-and-out flow on the bidirectional flow phosphorus removal filtration pool, so as to control the bidirectional flow phosphorus removal filtration pool to switch between an upward flow filtration adsorption mode for phosphorus removal and a downward flow filtration adsorption mode for phosphorus removal.

Inventors

Kuixiao LI
Yulong Shi
Qi Xu
Gang Wang
Jiawei WANG
Haipeng BAO
Guanglu Li
Fuliang MA

Assignees

Beijing Drainage Group Co., Ltd

Dates

Publication Date: 20260512
Application Date: 20211125
Priority Date: 20210623

Claims (10)

1 . A bidirectional flow pulse-based water body phosphorus removal apparatus, wherein the water body phosphorus removal apparatus comprises: a prefiltration unit, a bidirectional flow phosphorus removal filtration pool, a bidirectional water collection and distribution system, a filtration pool stratified gas pulse system, a water production tank and a control system; a filtration layer filled with a phosphorus removal filtration material is provided in the bidirectional flow phosphorus removal filtration pool; the control system is used for controlling the bidirectional water collection and distribution system to alternately perform upward water in-and-out flow and downward water in-and-out flow on the bidirectional flow phosphorus removal filtration pool, so as to control the bidirectional flow phosphorus removal filtration pool to switch between an upward flow filtration adsorption mode for phosphorus removal and a downward flow filtration adsorption mode for phosphorus removal; and the control system is used for controlling the filtration pool stratified gas pulse system to perform stratified pulse gas flushing on the filtration layer.
2 . The water body phosphorus removal apparatus according to claim 1 , wherein below the filtration layer, a lower water inlet and a lower water outlet are provided on the bidirectional flow phosphorus removal filtration pool, and above the filtration layer, an upper water inlet and an upper water outlet are provided on the bidirectional flow phosphorus removal filtration pool; the bidirectional water collection and distribution system comprises a water inlet pipe and a water production pipe; the water inlet pipe comprises a main water inlet pipe, a first water inlet branch pipe and a second water inlet branch pipe that are communicated with a water outlet end of the main water inlet pipe, a variable frequency pump is provided on the main water inlet pipe, the first water inlet branch pipe is communicated with the lower water inlet, and the second water inlet branch pipe is communicated with the upper water inlet; a fifth electric valve and a pressure transmitter are provided on the first water inlet branch pipe; a sixth electric valve is provided on the second water inlet branch pipe; the water production pipe comprises an upward flow water production branch pipe, a downward flow water production branch pipe, a primary produced water discharge pipe and a main water production pipe that are communicated with water outlet ends of the upward flow water production branch pipe and the downward flow water production branch pipe, respectively; a third electric valve is provided on the upward flow water production branch pipe; a fourth electric valve is provided on the downward flow water production branch pipe; the main water production pipe is communicated with the water production tank, and a second electric valve is provided thereon; the primary produced water discharge pipe is communicated with a water inlet pipe of the prefiltration unit, and a first electric valve is provided thereon; the apparatus comprises a water quality monitor and a liquid level gauge; the water quality monitor is configured to monitor the quality of water in the upward flow water production branch pipe and the downward flow water production branch pipe; the liquid level gauge is provided above the filtration layer in the apparatus; the control system is configured to control start and stop as well as operation frequency of the variable frequency pump, control the fifth electric valve and the sixth electric valve to be switched on or off, and compare a data signal of the water quality monitor with a preset value; when the data signal is greater than the preset value, the control system is configured to control the first electric valve to stay in a switched on state, and upward flow produced water or downward flow produced water flow back to the water inlet pipe of the prefiltration unit through the primary produced water discharge pipe for recycling treatment; when the data signal is equal to or less than the preset value, the control system is configured to control the second electric valve to stay in a switched on state, and upward flow produced water or downward flow produced water flow into the water production tank through the main water production pipe; the filtration pool stratified gas pulse system comprises a gas supply device and pulse units; each pulse unit comprises at least one group of pulse jet pipes, a connecting pipe for connecting the pulse jet pipes with the gas supply device, and a pulse valve provided on the connecting pipe; the pulse jet pipes are distributed in a height direction of the filtration layer, wherein the bottommost pulse jet pipe is positioned below the filtration layer and above the lower water inlet and the lower water outlet; when the bidirectional flow phosphorus removal filtration pool stays in an upward flow filtration adsorption mode, the control system is configured to control opening and closing of the gas supply device and the pulse valves to perform stratified pulse gas flushing on the filtration layer; the pulse jet pipes comprise main jet pipes and a plurality of branch jet pipes communicated with the main jet pipes; and a plurality of gas holes or a plurality of nozzles are provided on each of the main jet pipes, and a sieve made from an anti-corrosion material is provided on each of the gas holes or each of the nozzles.
3 . The water body phosphorus removal apparatus according to claim 2 , wherein the control system is configured to control the water inlet pipe to alternately perform upward water inflow and downward water inflow on the bidirectional flow phosphorus removal filtration pool according to a preset upward flow filtration time and a downward flow filtration time, or a pressure value detected by the pressure transmitter and a liquid level height in the apparatus detected by the liquid level gauge, so as to enable the bidirectional flow phosphorus removal filtration pool to switch between an upward flow filtration adsorption mode and a downward flow filtration adsorption mode; in the upward flow filtration adsorption mode, the variable frequency pump operates at a high frequency, the fifth electric valve is switched on, the sixth electric valve is switched off, and the control system is configured to compare a data signal of the pressure transmitter with a preset pressure value; when the data signal is less than the preset pressure value, the bidirectional flow phosphorus removal filtration pool maintains the upward flow filtration adsorption mode; when the data signal is greater than the preset pressure value, the control system is configured to control the variable frequency pump to operate at a low frequency, the fifth electric valve is switched off, the sixth electric valve is switched on, and the bidirectional flow phosphorus removal filtration pool is switched from the upward flow filtration adsorption mode to the downward flow filtration adsorption mode; in the downward flow filtration adsorption mode, the control system is configured to compare a data signal of the liquid level gauge with a preset liquid level value; when the data signal is less than the preset liquid level value, the bidirectional flow phosphorus removal filtration pool maintains the downward flow filtration adsorption mode; when the data signal is greater than the preset liquid level value, the control system is configured to control the variable frequency pump to operate at a high frequency, the fifth electric valve is switched on, the sixth electric valve is switched off, and the bidirectional flow phosphorus removal filtration pool is switched from the downward flow filtration adsorption mode to the upward flow filtration adsorption mode; \a water distributor (is provided at the top of the bidirectional flow phosphorus removal filtration pool; a filtration material regeneration lye inlet is provided on the bidirectional flow phosphorus removal filtration pool; the filtration material regeneration lye inlet and the upper water inlet are both communicated with the water distributor; the water quality monitor is configured to monitor a turbidity and a phosphate of the produced water in the upward flow water production branch pipe and the downward flow water production branch pipe; and \a bypass is provided on the pulse valve of each pulse unit, and a seventh electric valve is provided on the bypass and can be switched on when gas is continuously blown to the filtration layer.
4 . The water body phosphorus removal apparatus according to claim 2 , wherein the bidirectional flow phosphorus removal filtration pool operates in series of multiple stages, and three bidirectional flow phosphorus removal filtration pools operate in a mode that two bidirectional flow phosphorus removal filtration pools are connected in series of two stages and the third bidirectional flow phosphorus removal filtration pool is standby.
5 . The water body phosphorus removal apparatus according to claim 1 , wherein below the filtration layer, a lower water inlet and a lower water outlet are provided on the bidirectional flow phosphorus removal filtration pool, and above the filtration layer, an upper water inlet nd an upper water outlet are provided on the bidirectional flow phosphorus removal filtration pool; the bidirectional water collection and distribution system comprises a water inlet pipe and a water production pipe; the water inlet pipe comprises a main water inlet pipe, a first water inlet branch pipe and a second water inlet branch pipe that are communicated with a water outlet end of the main water inlet pipe; the first water inlet branch pipe is communicated with the lower water inlet, and a first power frequency pump and a fifth electric valve are provided thereon; the second water inlet branch pipe is communicated with the upper water inlet, and a second power frequency pump and a sixth electric valve are provided thereon; the water production pipe comprises an upward flow water production branch pipe, a downward flow water production branch pipe, a primary produced water discharge pipe and a main water production pipe that are communicated with water outlet ends of the upward flow water production branch pipe and the downward flow water production branch pipe, respectively; a third electric valve is provided on the upward flow water production branch pipe; a fourth electric valve (F 4 ) is provided on the downward flow water production branch pipe; the main water production pipe is communicated with the water production tank, and a second electric valve is provided thereon; the primary produced water discharge pipe is communicated with a water inlet pipe of the prefiltration unit, and a first electric valve is provided thereon; the apparatus comprises a water quality monitor and a liquid level gauge; the water quality monitor is configured to monitor the quality of water in the upward flow water production branch pipe and the downward flow water production branch pipe; the liquid level gauge is provided above the filtration layer in the apparatus; the control system is configured to control start and stop as well as operation frequency of the first power frequency pump and the second power frequency pump, control the fifth electric valve and the sixth electric valve to be switched on or off, and compare a data signal of the water quality monitor with a preset value; when the data signal is greater than the preset value, the control system is configured to control the first power frequency pump to start, the first electric valve stays in a switched on state, and upward flow produced water or downward flow produced water flow back to the water inlet pipe of the prefiltration unit through the primary produced water discharge pipe for recycling treatment; and when the data signal is equal to or less than the preset value, the control system is configured to control the second electric valve to stay in a switched on state, and upward flow produced water or downward flow produced water flow into the water production tank through the main water production pipe.
6 . A bidirectional flow pulse-based water body phosphorus removal method, wherein the water body phosphorus removal method is implemented in the water body phosphorus removal apparatus according to claim 1 , and the water body phosphorus removal method comprises the following steps: enabling water to be dephosphorized to flow through the prefiltration unit first to remove suspended solids therein, and enabling effluent water to flow into the bidirectional water collection and distribution system; controlling the bidirectional water collection and distribution system, by the control system, to alternately perform upward water inflow and downward water inflow, so as to enable the effluent water to flow into the bidirectional flow phosphorus removal filtration pool, and performing phosphorus removal by switching between an upward flow filtration adsorption mode and a downward flow filtration adsorption mode through the filtration layer; and meanwhile, controlling the filtration pool stratified gas pulse system, by the control system, to perform stratified pulse gas flushing on the filtration layer; when the bidirectional flow phosphorus removal filtration pool stays in the upward flow filtration adsorption mode, the control system controls the filtration pool stratified gas pulse system to perform stratified pulse gas flushing on the filtration layer; due to a pulse pressure and a gas jet volume of the filtration pool stratified gas pulse system, the phosphorus removal filtration material has an instantaneous expansion rate of 30-50%; and a pulse frequency of the filtration pool stratified gas pulse system is set according to a flow capacity of the filtration layer, a preset pulse period or an upward water inflow pressure.
7 . The water body phosphorus removal method according to claim 6 , the water body phosphorus removal method further comprises the following steps: S0, intercepting water to be dephosphorized by the prefiltration unit first to remove part of suspended solids therein, and enabling effluent water obtained after interception to flow into the bidirectional water collection and distribution system, wherein the effluent water obtained after interception has a turbidity of less than 1nephelometric turbidity unit (NTU); S1, controlling a water inlet pipe, by the control system, to perform upward water inflow, and enabling the effluent water obtained after interception to flow into the bidirectional flow phosphorus removal filtration pool through the lower water inlet; S2, controlling opening and closing of a gas supply device and a plurality of pulse valves, by the control system, to perform stratified pulse gas flushing on the filtration layer; S3, performing phosphorus removal on the effluent water obtained after interception by the bidirectional flow phosphorus removal filtration pool in an upward flow filtration adsorption mode, after the phosphorus removal is completed, enabling produced water to flow from a upper water outlet into a upward flow water production branch pipe and a main water production pipe, detecting the quality of the produced water by the water quality monitor, transmitting a data signal of the water quality monitor to a control system, and comparing the data signal with a preset value by the control system; when the signal is greater than the preset value, controlling a first electric valve to be switched on by the control system, and enabling the produced water to flow back to a water inlet pipe of the prefiltration unit through a primary produced water discharge pipe for recycling treatment; and otherwise, controlling a second electric valve to be switched on by the control system, and enabling the produced water to flow into a water production tank through the main water production pipe; S4, when the phosphorus removal is performed in the upward flow filtration adsorption mode for a first preset time or an upward water inflow pressure is greater than a preset pressure value, controlling the water inlet pipe, by the control system, to perform downward water inflow, and enabling the effluent water obtained after interception to flow into the bidirectional flow phosphorus removal filtration pool through an upper water inlet; performing phosphorus removal on the effluent water obtained after interception by the bidirectional flow phosphorus removal filtration pool in the downward flow filtration adsorption mode, after the phosphorus removal is completed, enabling produced water to flow from a lower water outlet into a downward flow water production branch pipe, detecting the quality of the produced water by the water quality monitor, transmitting a data signal of the water quality monitor to the control system, and comparing the data signal with a preset value by the control system; when the data signal is greater than the preset value, controlling the first electric valve to be switched on by the control system, and enabling the produced water to flow back to the water inlet pipe of the prefiltration unit through the primary produced water discharge pipe for recycling treatment; and otherwise, controlling the second electric valve to be switched on by the control system, and enabling the produced water to flow into the water production tank through the main water production pipe; and S5, when the phosphorus removal is performed in the downward flow filtration adsorption mode for a second preset time or the liquid level of the bidirectional flow phosphorus removal filtration pool is equal to or greater than a preset liquid level, repeating steps S1 to S4.
8 . The water body phosphorus removal method according to claim 7 , further comprising: in step S1, controlling the water inlet pipe, by the control system, to perform upward water inflow means that the control system controls a variable frequency pump to operate and a fifth electric valve to be switched on, and the effluent water obtained after interception flows from the lower water inlet into the bidirectional flow phosphorus removal filtration pool through the main water inlet pipe and the first water inlet branch pipe; in step S4, controlling the water inlet pipe, by the control system, to perform downward water inflow means that the control system controls the variable frequency pump to operate, the fifth electric valve to be switched off and a sixth electric valve to be switched on, and the effluent water obtained after interception flows from the upper water inlet into the bidirectional flow phosphorus removal filtration pool through the main water inlet pipe and a second water inlet branch pipe; the water body phosphorus removal method further comprises regenerating the phosphorus removal filtration material; and pulse gas blowing is continuously performed on the filtration layer by the filtration pool stratified gas pulse system, or stratified gas flushing is continuously performed on the filtration layer by switching on the electric valves on the bypasses of the pulse valves.
9 . The water body phosphorus removal method according to claim 7 , further comprising: in step S1, controlling the water inlet pipe, by the control system, to perform upward water inflow means that the control system controls a first power frequency pump to operate and a fifth electric valve to be switched on, and the effluent water obtained after interception flows from the lower water inlet into the bidirectional flow phosphorus removal filtration pool through a main water inlet pipe and a first water inlet branch pipe; in step S4, controlling the water inlet pipe, by the control system, to perform downward water inflow means that the control system controls the first power frequency pump to close, the fifth electric valve to be switched off, a second power frequency pump to operate and a sixth electric valve to be switched on, and the effluent water obtained after interception flows from the upper water inlet into the bidirectional flow phosphorus removal filtration pool through the main water inlet pipe and a second water inlet branch pipe; and in a case that the water body phosphorus removal apparatus comprises three bidirectional flow phosphorus removal filtration pools in series, two bidirectional flow phosphorus removal filtration pools operate in series, and the third bidirectional flow phosphorus removal filtration pool is in standby.
10 . An organic nutrient soil, wherein the organic nutrient soil is prepared by using a phosphorus-rich solution obtained by regeneration of the phosphorus removal filtration material in the method according to claim 9 ; and the organic nutrient soil is prepared by using anaerobic digestion sludge of a reclaimed water plant as a raw material and the phosphorus-rich solution as a phosphorus source additive.

Description

FIELD OF TECHNOLOGY The present disclosure belongs to the technical field of sewage treatment, and more specifically relates to a bidirectional flow pulse-based water body phosphorus removal apparatus and a method, and an organic nutrient soil. BACKGROUND Phosphorus is a mineral element necessary for humans to maintain life activities and production activities. The phosphorus exists in phosphate rock ores and is not a natural renewable resource on earth. It has been reported that the amount of mineable phosphate ores in the world is about 7 billion tons. With continuous increase of the population, the phosphorus is increasingly consumed every year. When the phosphorus is increasingly consumed at a rate of 2% per year, phosphate ore reserves can only be used by humans for about 100 years. Therefore, more and more attention has been paid to resource recycling of the phosphorus by governments of various countries around the world. Recovery of phosphorus from a reclaimed water plant is a key link of a social cycle of phosphorus. Phosphorus in effluent water of the reclaimed water plant is an important phosphorus source in receiving water. At present, the annual output of reclaimed water in Beijing is about 1 billion cubic meters, in which nearly 80% is reused as water in landscape environments. Although the content (TP<0.3 mg/L) of phosphorus in the reclaimed water satisfies “Discharge Standard of Reclaimed Water Pollutants for Municipal Wastewater Treatment Plants” (DB11/890-2012), the phosphorus concentration level in the reclaimed water discharge standard is far greater than the phosphorus concentration level (TP<0.025 mg/L) required for maintaining a good water environment based on evaluation criteria for nutrient levels of lakes stipulated by the Environmental Protection Agency (EPA) of the United States. Excessive content of the phosphorus in water will accelerate algae reproduction, leading to eutrophication, decrease of dissolved oxygen concentration in water and anoxic death of aquatic organisms, thereby seriously damaging the ecological environment. Therefore, deep phosphorus removal and phosphorus recovery of reclaimed water can not only maintain a good water ecological environment, but also realize sustainable utilization of phosphorus resources. Adsorption for phosphorus removal is an effective method for deep phosphorus removal. At present, most of artificially synthetic phosphorus removal filtration materials are metal oxides and composite materials thereof, and most of phosphorus removal filtration pools use a downward flow filtration mode. It has been found during long-term operation that a filtration layer in a downward flow phosphorus removal filtration pool is prone to the problems of blocking and hardening, and due to the monotonous downward flow filtration mode, the adsorption capacity of a filtration material at a lower part of the filtration layer cannot be fully utilized. SUMMARY The purpose of the present disclosure is to provide a bidirectional flow pulse-based water body phosphorus removal apparatus and a method, and an organic nutrient soil. The apparatus can prevent the problems of blocking and hardening of a filtration layer by switching between an upward flow filtration adsorption mode and a downward flow filtration adsorption mode, and the adsorption capacity of the filtration layer can be fully utilized. In order to realize the above purpose, in a first aspect, the present disclosure provides a bidirectional flow pulse-based water body phosphorus removal apparatus. The water body phosphorus removal apparatus includes: a prefiltration unit, a bidirectional flow phosphorus removal filtration pool, a bidirectional water collection and distribution system, a filtration pool stratified gas pulse system, a water production tank and a control system; a filtration layer filled with a phosphorus removal filtration material is provided in the bidirectional flow phosphorus removal filtration pool;the control system is used for controlling the bidirectional water collection and distribution system to alternately perform upward water in-and-out flow and downward water in-and-out flow on the bidirectional flow phosphorus removal filtration pool, so as to control the bidirectional flow phosphorus removal filtration pool to switch between an upward flow filtration adsorption mode for phosphorus removal and a downward flow filtration adsorption mode for phosphorus removal;the control system is used for controlling the filtration pool stratified gas pulse system to perform stratified pulse gas flushing on the filtration layer. Specifically, below the filtration layer, a lower water inlet and a lower water outlet are provided on the bidirectional flow phosphorus removal filtration pool, and above the filtration layer, an upper water inlet and an upper water outlet are provided on the bidirectional flow phosphorus removal filtration pool; the bidirectional water collection and distribution system