CN104772095B - Automatically regulate chloramines preparation facilities and the method thereof of pharmacy response usage ratio according to variations in temperature - Google Patents

Automatically regulate chloramines preparation facilities and the method thereof of pharmacy response usage ratio according to variations in temperature Download PDF

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Publication number
CN104772095B
CN104772095B CN201510112260.2A CN201510112260A CN104772095B CN 104772095 B CN104772095 B CN 104772095B CN 201510112260 A CN201510112260 A CN 201510112260A CN 104772095 B CN104772095 B CN 104772095B
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chloramines
liquid level
main control
reserve tank
tank
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CN104772095A (en
Inventor
柳景青
申屠华斌
罗志逢
周晓燕
裘尚德
何晓芳
叶萍
胡宝兰
楼莉萍
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Co Ltd Of Water Surrounding Research Institute Of Shaoxin City
Jiaxing City Jia Yuan Plumbing Co Ltd
Zhejiang University ZJU
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Co Ltd Of Water Surrounding Research Institute Of Shaoxin City
Jiaxing City Jia Yuan Plumbing Co Ltd
Zhejiang University ZJU
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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Accessories For Mixers (AREA)

Abstract

The invention discloses a kind of chloramines preparation facilities and method thereof that automatically regulates pharmacy response usage ratio according to variations in temperature, this device comprises pharmacy response stocking system, chloramines generation system, chloramines stocking system, control system and bracing frame, pharmacy response stocking system is made up of ammonium chloride reserve tank and clorox reserve tank, control system comprises PLC Main Control Tank and coupled temperature sensor, motor-driven valve, measuring pump and liquid level sensor, chloramines generation system is made up of chloramines reaction chamber and electric mixer, chloramines generation system is connected with stainless steel tube with chloramines stocking system, and the UNICOM's state between motor-driven valve control two systems is set, chloramines stocking system is added to chloramines in water supply network by measuring pump. the present invention is applicable to the continuous production of chloramines disinfection agent in the feedwater water factory of city or small towns and quantitatively adds, and is not subject to the impact of variation of ambient temperature, and the chloramines concentration stabilize making, prepares and to add automaticity high, simple to operate, easy to maintenance.

Description

Automatically regulate chloramines preparation facilities and the method thereof of pharmacy response usage ratio according to variations in temperature
Technical field
The present invention relates to a kind of chloramines preparation facilities and method thereof that automatically regulates pharmacy response usage ratio according to variations in temperature. Relate in particular to a kind of chloramines preparation facilities and method thereof that automatically regulates ammonium chloride and clorox usage ratio according to variations in temperature.
Background technology
Liquid chlorine is during as disinfectant, because its cost is reliably widely used compared with low, technical maturity, effect stability. But chlorine is hypertoxic dangerous material, the steel cylinder of storage chlorine belongs to high-pressure bottle, has potential threat, and can react with free chlorine generation carcinogen (as haloform) when organic matter is more in water. And Comparatively speaking, chloramines as disinfectant advantage more as: in (1) chloramines and water humic substance effect less, the therefore general little generation haloform of chloramines disinfection (THMS) and halogen acetic acid (HAAS), generation Cancer-causing mutation compound also fewer. (2) good stability of chloramines, penetration capacity is stronger than chlorine, duration in pipe network is long, can effectively control breeding and the biomembranous formation of harmful substance microorganism in pipe network, sterilization persistence is strong, thereby can effectively suppress the breeding of remaining bacterium, more can ensure the requirement of the residual chlorine amount of pipe network. (3) chloramines disinfection is to be had an effect by the HClO slowly releasing, therefore oxidability comparatively speaking a little less than the rate of exchange, can slow down the residual stink of liquid chlorine disinfection greatly. (4) chloramines disinfection is less to the corrosivity of water supply network.
In recent years, due to the regulation of the concern to DBPs DBPS and Disinfection Byproducts in Drinking Water restriction, more and more water factories adopt chloramines to replace liquid chlorine disinfection as disinfectant. At present, preparation chloramines adopts artificial preparation then to add mostly, and the generation concentration of still adopting the chloramines of preparing is in this way subject to the impact of environment temperature, is unfavorable for quantitatively adding of disinfectant. For addressing the above problem, a kind of chloramines preparation facilities that automatically regulates pharmacy response (ammonium chloride solution and liquor natrii hypochloritis) usage ratio according to variations in temperature of design.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, a kind of chloramines preparation facilities and method thereof that automatically regulates pharmacy response usage ratio according to variations in temperature is provided.
Automatically regulate the chloramines preparation facilities of pharmacy response usage ratio to comprise pharmacy response stocking system according to variations in temperature, chloramines generation system, chloramines stocking system, control system and supporting seat, pharmacy response stocking system is made up of ammonium chloride reserve tank and clorox reserve tank, each reserve tank all arranges liquid level tube and blow-down pipe, gate valve control is installed on blow-down pipe to be opened and closed, chloramines generation system is made up of chloramines reaction chamber and electric mixer, in chloramines reaction chamber, electric mixer is installed, chloramines reaction chamber arranges blow-down pipe and liquid level tube, gate valve control is installed on blow-down pipe to be opened and closed, chloramines stocking system is made up of chloramines reserve tank and No. 3 measuring pumps, chloramines reserve tank is connected by plastic flexible pipe with No. 3 measuring pumps, chloramines reserve tank arranges liquid level tube and sampling pipe, gate valve control is installed on sampling pipe to be opened and closed, the temperature sensor that control system comprises PLC Main Control Tank and is connected with PLC Main Control Tank, motor-driven valve, No. 1 measuring pump, No. 2 measuring pumps and liquid level sensor, bracing frame is to be made up of stainless steel stent, pharmacy response stocking system is connected with chloramines reaction chamber with No. 2 measuring pumps by No. 1 measuring pump of PLC Main Control Tank control, chloramines generation system is connected by stainless steel tube with chloramines stocking system, and the UNICOM's state between motor-driven valve control two systems is set, chloramines stocking system is added to chloramines in water supply network by No. 3 measuring pumps.
Described clorox reserve tank, ammonium chloride reserve tank, chloramines reaction chamber, chloramines reserve tank are all stainless steel, and their volumetric ratio is 3:1:1:1. Described electric mixer is three leaf propeller mixers.
Described chloramines preparation facilities regulates the method for pharmacy response usage ratio to be according to variations in temperature automatically: in described PLC Main Control Tank, pre-deposit under different temperatures and to generate the pharmacy response usage ratio curve of stablizing chloramines concentration, the real time temperature detecting is fed back to PLC Main Control Tank by described temperature sensor, PLC Main Control Tank is according to the consumption that generates the pharmacy response change curve of stablizing chloramines concentration under the different temperatures depositing in and calculate ammonium chloride and clorox, in chloramines reaction chamber, add ammonium chloride and clorox medicament according to the order of nitrogen after first chlorine according to the consumption calculating, reinforced process realizes by the operation of No. 1 measuring pump of PCL Main Control Tank control and No. 2 measuring pumps, whole process control is in 10min, electric mixer on described chloramines reaction chamber is after pharmacy response adds, open and stir 10min, leave standstill 20min, after reaction finishes, motor-driven valve is opened, the medicament generating enters into chloramines reserve tank, in the time that the liquid level sensor of chloramines reserve tank detects high liquid level, electrically operated valve is closed, simultaneously, No. 3 measuring pumps start and by the adding of agent generating in water supply network,
Described PCL Main Control Tank is provided with automatic transmission and manual, and the duty of chloramines preparation facilities can be switched. The dosage of described stirring and standing time, pharmacy response, the dosage of generation medicament all manually arrange by the touch-screen on PCL Main Control Tank. Described liquid level sensor is in time feeding back to PLC Main Control Tank by signal when the liquid level of chloramines reserve tank during lower than low liquid level, device starts to rework, equally, the medicament generating in case when chloramines leads in the process in chloramines reserve tank, when liquid level in chloramines reserve tank reaches high liquid level, signal is passed to PCL Main Control Tank by liquid level sensor, and then motor-driven valve cuts out. After once described No. 3 measuring pumps are opened, all the time with the flow set continuously to the disinfectant that adds in water supply network. The disinfectant chloramines change in concentration error that described chloramines preparation facilities generates is controlled within the scope of 1-5%.
Advantage of the present invention has: the consumption that 1) can automatically regulate with the variation of environment temperature pharmacy response ammonium chloride and clorox; 2) the chloramines concentration of preparing maintains all the time certain concentration level so that quantitatively adding disinfectant; 3) chloramines that need add for a day can be prepared several times in order to avoid place and cause its concentration to decay because the disposable chloramines making is long-time.
Brief description of the drawings
Fig. 1 is chloramines setting plane of the present invention;
Fig. 2 is the A-A profile of Fig. 1 of the present invention;
Fig. 3 is the B-B profile of Fig. 1 of the present invention;
In chloramines setting plane, A-A profile, B-B section: clorox reserve tank 1, ammonium chloride reserve tank 2, chloramines reaction chamber 3, chloramines reserve tank 4,7, No. 3 measuring pumps 8 of 6, No. 2 measuring pumps of 5, No. 1 measuring pump of PCL Main Control Tank, temperature sensor 9, electric mixer 10, motor-driven valve 11, gate valve 12, liquid level sensor 13, liquid level tube 14, stainless steel stent 15, three-way connection 16, blow-down pipe 17, sampling pipe 18.
Detailed description of the invention
As shown in accompanying drawing 1-3, automatically regulate the chloramines preparation facilities of pharmacy response usage ratio to comprise pharmacy response stocking system according to temperature variations in temperature, chloramines generation system, chloramines stocking system, control system and supporting seat, pharmacy response stocking system is made up of ammonium chloride reserve tank and clorox reserve tank, each reserve tank all arranges liquid level tube and blow-down pipe, gate valve control is installed on blow-down pipe to be opened and closed, chloramines generation system is made up of chloramines reaction chamber and minitype electric mixer, in chloramines reaction chamber, electric mixer is installed, chloramines reaction chamber arranges blow-down pipe and liquid level tube, gate valve control is installed on blow-down pipe to be opened and closed, chloramines stocking system is made up of chloramines reserve tank and No. 3 measuring pumps, chloramines reserve tank is connected by plastic flexible pipe with No. 3 measuring pumps, chloramines reserve tank arranges liquid level tube and sampling pipe, gate valve control is installed on sampling pipe to be opened and closed, the temperature sensor that control system comprises PLC Main Control Tank and is connected with PLC Main Control Tank, motor-driven valve, No. 1 measuring pump, No. 2 measuring pumps and liquid level sensor, supporting seat is made up of stainless steel stent, pharmacy response stocking system is connected with chloramines reaction chamber with No. 2 measuring pumps by No. 1 measuring pump of PLC Main Control Tank control, chloramines generation system is connected by stainless steel tube with chloramines stocking system, and the UNICOM's state between motor-driven valve control two systems is set, chloramines stocking system is added to chloramines in water supply network by No. 3 measuring pumps.
Described clorox reserve tank, ammonium chloride reserve tank, chloramines reaction chamber, chloramines reserve tank are all stainless steel, and their volumetric ratio is 3:1:1:1. in described PLC Main Control Tank, pre-deposit under different temperatures and to generate the pharmacy response usage ratio curve of stablizing chloramines concentration, the real time temperature detecting is fed back to PLC Main Control Tank by described temperature sensor, PLC Main Control Tank is according to the consumption that generates the pharmacy response change curve of stablizing chloramines concentration under the different temperatures depositing in and calculate ammonium chloride and clorox, in chloramines reaction chamber, add ammonium chloride and clorox medicament according to the order of nitrogen after first chlorine according to the consumption calculating, reinforced process realizes by the operation of No. 1 measuring pump of PCL Main Control Tank control and No. 2 measuring pumps, whole process control is in 10min, electric mixer on described chloramines reaction chamber is after pharmacy response adds, open and stir 10min, leave standstill 20min, after reaction finishes, motor-driven valve is opened, the medicament generating enters into chloramines reserve tank, in the time that the liquid level sensor of chloramines reserve tank detects high liquid level, No. 3 measuring pumps open and by the adding of agent generating in water supply network, described PCL Main Control Tank is provided with automatic transmission and manual, the duty of chloramines preparation facilities can be switched. the dosage of described stirring and standing time, pharmacy response, the dosage of generation medicament all manually arrange by the touch-screen on PCL Main Control Tank, after once No. 3 described measuring pumps are opened, all the time with the flow set continuously to the disinfectant that adds in water supply network, the disinfectant chloramines change in concentration error that described chloramines preparation facilities generates is controlled within the scope of 1-5%.
After device is opened, be fixed on temperature sensor 9 on liquor natrii hypochloritis's reserve tank 1 by measured temperature feedback to PLC Main Control Tank 5, PLC Main Control Tank 5 calculates the consumption of needed pharmacy response according to the chloramines concentration curve generating under the different temperatures of input, then by controlling 6 and No. 2 measuring pumps 7 of No. 1 measuring pump, pharmacy response is added in chloramines reaction chamber 3, after adding, start electric mixer 10, stir 10min, leave standstill 20min, reaction finishes. Opening motor-driven valve 11 makes the medicament generating enter into chloramines reserve tank 4, when the liquid level sensor 13 in chloramines reserve tank 4 monitors in the time that liquid level reaches 0.25m, signal is passed to PCL Main Control Tank 5, then closing 11, No. 3 measuring pumps 8 of motor-driven valve starts working the medicament of generation is quantitatively added continuously. When the liquid level in chloramines storage box 4 is during lower than 0.1m, signal is passed to PCL Main Control Tank 5 by liquid level sensor 13, and then PCL Main Control Tank 5 repeats last action process, realizes the continuous production of chloramines.

Claims (6)

1. a chloramines preparation facilities regulates the method for pharmacy response usage ratio automatically according to variations in temperature, described chloramines preparation facilities comprises pharmacy response stocking system, chloramines generation system, chloramines stocking system, control system and supporting seat, pharmacy response stocking system is made up of ammonium chloride reserve tank (1) and clorox reserve tank (2), each reserve tank all arranges liquid level tube (14) and blow-down pipe, gate valve (12) is installed on blow-down pipe and is controlled switching, chloramines generation system is made up of chloramines reaction chamber (3) and electric mixer (10), electric mixer (10) is installed in chloramines reaction chamber (3), chloramines reaction chamber (3) arranges blow-down pipe and liquid level tube (14), gate valve (12) is installed on blow-down pipe and is controlled switching, chloramines stocking system is made up of chloramines reserve tank (5) and No. 3 measuring pumps (8), chloramines reserve tank (5) is connected by plastic flexible pipe with No. 3 measuring pumps (8), chloramines reserve tank (4) arranges liquid level tube (15) and sampling pipe (18), gate valve (12) is installed on sampling pipe and is controlled switching, the temperature sensor (9) that control system comprises PLC Main Control Tank (5) and is connected with PLC Main Control Tank (5), motor-driven valve (11), No. 1 measuring pump (6), No. 2 measuring pumps (7) and liquid level sensor (13), bracing frame is to be made up of stainless steel stent (3), No. 1 measuring pump (6) that pharmacy response stocking system is controlled by PLC Main Control Tank (5) is connected with chloramines reaction chamber (3) with No. 2 measuring pumps (7), chloramines generation system is connected by stainless steel tube with chloramines stocking system, and motor-driven valve (11) is set controls the UNICOM's state between two systems, chloramines stocking system is added to chloramines in water supply network by No. 3 measuring pumps (8),
It is characterized in that: in described PLC Main Control Tank (5), pre-deposit under different temperatures and to generate the pharmacy response usage ratio curve of stablizing chloramines concentration, the real time temperature detecting is fed back to PLC Main Control Tank (5) by described temperature sensor (9), PLC Main Control Tank (5) is according to the consumption that generates the pharmacy response change curve of stablizing chloramines concentration under the different temperatures depositing in and calculate ammonium chloride and clorox, in chloramines reaction chamber (3), add ammonium chloride and clorox medicament according to the order of nitrogen after first chlorine according to the consumption calculating, the operation that reinforced process is controlled No. 1 measuring pump (6) and No. 2 measuring pumps (7) by PCL Main Control Tank (5) realizes, whole process control is in 10min, electric mixer (10) on described chloramines reaction chamber (3) is after pharmacy response adds, open and stir 10min, leave standstill 20min, after reaction finishes, motor-driven valve (16) is opened, the medicament generating enters into chloramines reserve tank (4), in the time that the liquid level sensor (13) of chloramines reserve tank (4) detects high liquid level, electrically operated valve (16) is closed, simultaneously, No. 3 measuring pumps (8) start and by generate adding of agent in water supply network.
2. method according to claim 1, is characterized in that: described PCL Main Control Tank (10) is provided with automatic transmission and manual, and the duty of chloramines preparation facilities can be switched.
3. method according to claim 1, is characterized in that: the dosage of described stirring and standing time, pharmacy response, the dosage of generation medicament all manually arrange by the touch-screen on PCL Main Control Tank (10).
4. method according to claim 1, it is characterized in that: described liquid level sensor (18) is in time feeding back to PLC Main Control Tank (10) by signal when the liquid level of chloramines reserve tank (9) during lower than low liquid level, device starts to rework, equally, the medicament generating in case (8) when chloramines leads in the process in chloramines reserve tank (9), when liquid level in chloramines reserve tank (9) reaches high liquid level, signal is passed to PCL Main Control Tank (10) by liquid level sensor, and then motor-driven valve (16) cuts out.
5. method according to claim 1, is characterized in that: described No. 3 measuring pumps (13) once after opening, all the time with the flow set continuously to the disinfectant that adds in water supply network.
6. method according to claim 1, is characterized in that: the disinfectant chloramines change in concentration error that described chloramines preparation facilities generates is controlled within the scope of 1-5%.
CN201510112260.2A 2015-03-16 2015-03-16 Automatically regulate chloramines preparation facilities and the method thereof of pharmacy response usage ratio according to variations in temperature Active CN104772095B (en)

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CN106622011A (en) * 2016-11-17 2017-05-10 天津滨海光热反射技术有限公司 A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4867375A (en) * 1987-12-17 1989-09-19 Matsushita Electric Industrial Co., Ltd. Temperature-adjustable water supply system
CN103100334A (en) * 2013-02-28 2013-05-15 徐州五洋科技股份有限公司 Emulsified liquid supplying system for underground coal mine
CN103736421A (en) * 2013-12-27 2014-04-23 新昌县奇鹏自动化设备有限公司 Method for preparing narcotic by using system with temperature regulating device and controller

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4867375A (en) * 1987-12-17 1989-09-19 Matsushita Electric Industrial Co., Ltd. Temperature-adjustable water supply system
CN103100334A (en) * 2013-02-28 2013-05-15 徐州五洋科技股份有限公司 Emulsified liquid supplying system for underground coal mine
CN103736421A (en) * 2013-12-27 2014-04-23 新昌县奇鹏自动化设备有限公司 Method for preparing narcotic by using system with temperature regulating device and controller

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