CN209196229U - A kind of wet device of new gas control oxygen control - Google Patents

A kind of wet device of new gas control oxygen control Download PDF

Info

Publication number
CN209196229U
CN209196229U CN201822216725.0U CN201822216725U CN209196229U CN 209196229 U CN209196229 U CN 209196229U CN 201822216725 U CN201822216725 U CN 201822216725U CN 209196229 U CN209196229 U CN 209196229U
Authority
CN
China
Prior art keywords
level
triple valve
humidifier
tempering tank
control
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201822216725.0U
Other languages
Chinese (zh)
Inventor
胡天明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FOSHAN FASTECH Co Ltd
Original Assignee
FOSHAN FASTECH Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by FOSHAN FASTECH Co Ltd filed Critical FOSHAN FASTECH Co Ltd
Priority to CN201822216725.0U priority Critical patent/CN209196229U/en
Application granted granted Critical
Publication of CN209196229U publication Critical patent/CN209196229U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of wet device of new gas control oxygen control, including sequentially connected level-one triple valve, drier, level-one tempering tank, humidifier, second level triple valve and second level tempering tank, the level-one triple valve passes through piping connection oxygen analyser, by piping connection hygrometer, the level-one triple valve, oxygen analyser, second level triple valve, hygrometer are electrically connected with PLC controller the second level tempering tank respectively;One of air inlet pipeline of the second level triple valve connects humidifier, another air inlet pipeline is directly connected to level-one tempering tank.The dry of gas, wet gas current ratio are controlled by second level triple valve, guarantee moisture stable, by keeping gas to contain a certain amount of moisture humidity, it is more advantageous to steel wire rod surface treatment, it is controlled using gas mass flow, control dry and wet flow is calculated by degree, achievees the purpose that accurately to control humidity and oxygen content.

Description

A kind of wet device of new gas control oxygen control
Technical field
The utility model relates to a kind of mechanical equipment technical fields, and in particular to a kind of wet device of new gas control oxygen control.
Background technique
When wire rod is processed, it is initially formed chain base, line is made in casting or powder metallurgic method (refractory metal) chain base processed, second step Bar, forging, groove rolling (mainstream of production) squeeze, directly cast line bar, be eventually fabricated wire rod, when being made wire rod mostly by It draws, the big non-hard state wire rod of slicker solder welding wire section is once obtained by extrusion or continuously extruded legal system ear fork, wire rod exist When processing, generally require to carry out Surface heat-treatent, the purpose is to obtain the superficial layer of high rigidity and the distribution of advantageous internal stress, with The wear-resisting property and anti-fatigue performance of workpiece are improved, gas needs a kind of dioxy that control oxygen control is wet when wire rod finished surface is heat-treated Change carbon protective atmosphere, for traditional equipment when controlling gas humidity, structure is more complicated, and precision is bad.
Utility model content
It is simple and can to provide a kind of structure for the shortcomings that the purpose of the utility model is to overcome the prior arts and insufficient The device of accurate control oxygen concentration and humidity.
The purpose of this utility model is achieved through the following technical solutions: a kind of wet device of new gas control oxygen control, including according to Level-one triple valve, drier, level-one tempering tank, humidifier, second level triple valve and the second level tempering tank of secondary connection, the level-one three Port valve passes through piping connection hygrometer, the level-one triple valve, oxygen determination by piping connection oxygen analyser, the second level tempering tank Instrument, second level triple valve, hygrometer are electrically connected with PLC controller respectively;The level-one triple valve, second level threeway valve arrangement are the same, Respectively include motor, valve body, spool, two air inlet pipelines and an outlet pipe, the shape of the spool is shuttle shape, in valve body Shuttle shape movable chamber equipped with spool, two air inlet pipelines are separately connected two opposite ends of shuttle shape movable chamber, and outlet pipe connects Connect the middle part of shuttle shape movable chamber;One of air inlet pipeline of the second level triple valve connects humidifier, another air inlet pipeline It is directly connected to level-one tempering tank.
In above scheme, the humidifier includes the first humidifier, the second humidifier and small pump, the small pump difference Pass through the first humidifier of piping connection, the second humidifier.
The utility model compared with the existing technology have following advantages and effects
PLC controller is finely adjusted the oxygen content value in dry air by level-one triple valve, guarantees oxygen content ratio Example is correct, realizes the purpose of control oxygen content, and be capable of the flow of valve two kinds of gas of control, simplifies device;Pass through two Dry, the wet gas current ratio of grade triple valve control gas, guarantees moisture stable, wet by keeping gas to contain a certain amount of moisture Degree is more advantageous to steel wire rod surface treatment, is controlled using gas mass flow, is calculated control dry and wet flow by degree, is reached The purpose of accurate control humidity and oxygen content, improves wire rod processing quality, improves wire rod processing efficiency;Device overall structure compares Simply, internal process is simplified, save the cost is simultaneously and maintenance cost is low, and practical performance increases.
Detailed description of the invention
1- level-one triple valve;2- oxygen analyser;3- drier;4- level-one tempering tank;5-PLC controller;6- second level triple valve; 7- humidifier;8- second level tempering tank;9- hygrometer;10- motor;11- valve body;12- pipeline;13- shuttle shape movable chamber;14- spool; 15- outlet pipe;16- pipeline;The first humidifier of 71-;The second humidifier of 72-;73- small pump.
Fig. 1 is the overall structure figure of the wet device of new gas control oxygen control.
Fig. 2 is the structure chart of I and II triple valve.
Specific embodiment
The present invention will be further described in detail with reference to the embodiments and the accompanying drawings, but the implementation of the utility model Mode is without being limited thereto.
Referring to Figures 1 and 2, the wet device of a kind of new gas control oxygen control, including sequentially connected level-one triple valve 1, drying Device 3, level-one tempering tank 4, humidifier 7, second level triple valve 6 and second level tempering tank 8, the level-one triple valve 1 pass through piping connection Oxygen analyser 2, the second level tempering tank 6 pass through piping connection hygrometer 9, the level-one triple valve 1, oxygen analyser 2, second level triple valve 6, hygrometer 9 is electrically connected with PLC controller 5 respectively;The level-one triple valve 1,6 structure of second level triple valve are the same, respectively include There are one outlet pipes 15 for 14, two motor 10, valve body 11, spool air inlet pipelines, on the diagram, air inlet pipeline are as follows: pipeline 12 With pipeline 16;The shape of the spool 14 is shuttle shape, and the shuttle shape movable chamber 13 of spool 14, two air inlets are equipped in valve body 11 Pipeline, pipeline 12 and pipeline 16 are separately connected two opposite ends of shuttle shape movable chamber 14, and outlet pipe 15 connects shuttle shape movable chamber 13 Middle part, principle is: motor 10 by PLC controller 5 control band movable valve plug 14 up or down move, when spool 14 is past When upper movement, 16 air inlet of pipeline of top is reduced, and pipeline 12 air inlet in lower section increases, and is controlled so as to meet a spool 14 The ratio of oxygen, carbon dioxide simplifies structure;One of air inlet pipeline of the second level triple valve 6 connects humidifier 7, separately One air inlet pipeline is directly connected to level-one tempering tank 4.
Working principle: PLC controller 5 sets the content value of oxygen, so as to adjust in level-one triple valve 1 motor 10 it is dynamic Make, the aeration ratio of oxygen and carbon dioxide is made to keep corresponding with setting value, if there is deviation, oxygen analyser 2 can turn oxygen content Chemical conversion 4-20mA signal gives PLC controller 5, and is compared by PLC controller with oxygen content, if there is deviation feeding to give one Grade triple valve 1 controls signal, continues the spool 14 for adjusting level-one triple valve 1;Oxygen, the carbon dioxide gas mixture of proportions constant After being further dried into drier 3, level-one tempering tank 4 is reached, and be divided into two-way, directly reaches second level triple valve all the way 6 one of air inlet pipeline, another way connect humidifier 7, and distilled water is filled in water controller 7, mixed gas after being bubbled, It generates small bubble and is sufficiently combined with moisture, become saturated with moisture stream, and be sent to another air inlet pipe of second level triple valve 6 Road finally reaches second level tempering tank 8, and for second level tempering tank 8 after the measurement of hygrometer 9, hygrometer 9 converts gas humidity value It is fed back in PLC controller 5 for 4-20mA signal, and be compared with setting value, if it exists deviation, it will by PLC controller 5 Deviation calculates output to second level triple valve 6, so that control is dry, wet gas current ratio, guarantees moisture stable, by keeping gas Body contains a certain amount of moisture humidity, is more advantageous to steel wire rod surface treatment, is controlled using gas mass flow, by degree meter Control dry and wet flow is calculated, achievees the purpose that accurately to control humidity and oxygen content, improves wire rod processing quality, improves wire rod processing effect Rate, it is practical.
Preferably, the humidifier 7 includes the first humidifier 71, the second humidifier 73 and small pump 72, the small pump 73 pass through piping connection the first humidifier 71, the second humidifier 73 respectively.
Above-described embodiment is the preferable embodiment of the utility model, but the embodiments of the present invention is not by above-mentioned The limitation of embodiment, it is made under other any spiritual essence and principles without departing from the utility model to change, modify, replacing In generation, simplifies combination, should be equivalent substitute mode, is included within the protection scope of the utility model.

Claims (2)

1. a kind of wet device of new gas control oxygen control, which is characterized in that including sequentially connected level-one triple valve, drier, one Grade tempering tank, humidifier, second level triple valve and second level tempering tank, the level-one triple valve are described by piping connection oxygen analyser Second level tempering tank by piping connection hygrometer, the level-one triple valve, oxygen analyser, second level triple valve, hygrometer respectively with PLC Controller electrical connection;The level-one triple valve, second level threeway valve arrangement are the same, respectively include motor, valve body, spool, two into Air pipe and an outlet pipe, the shape of the spool are shuttle shape, the shuttle shape movable chamber of spool are equipped in valve body, described in two Air inlet pipeline is separately connected two opposite ends of shuttle shape movable chamber, and outlet pipe connects the middle part of shuttle shape movable chamber;The second level three One of air inlet pipeline of port valve connects humidifier, another air inlet pipeline is directly connected to level-one tempering tank.
2. the wet device of new gas control oxygen control according to claim 1, which is characterized in that the humidifier adds including first Wet device, the second humidifier and small pump, the small pump pass through the first humidifier of piping connection, the second humidifier respectively.
CN201822216725.0U 2018-12-27 2018-12-27 A kind of wet device of new gas control oxygen control Active CN209196229U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822216725.0U CN209196229U (en) 2018-12-27 2018-12-27 A kind of wet device of new gas control oxygen control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822216725.0U CN209196229U (en) 2018-12-27 2018-12-27 A kind of wet device of new gas control oxygen control

Publications (1)

Publication Number Publication Date
CN209196229U true CN209196229U (en) 2019-08-02

Family

ID=67430662

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822216725.0U Active CN209196229U (en) 2018-12-27 2018-12-27 A kind of wet device of new gas control oxygen control

Country Status (1)

Country Link
CN (1) CN209196229U (en)

Similar Documents

Publication Publication Date Title
CN103771553B (en) The adaptive fuzzy control method of wet flue gas desulfurization waste water evaporation process
DE102009019838B4 (en) A fuel cell system and method for determining the speed of a recirculation pump in an anode recirculation circuit of a fuel cell system
CN102798565B (en) Gas distribution device utilizing saturated steam method to simulate exhalation gas alcohol content and concentration algorithm thereof
CN106277383B (en) Aeration control system and method based on oxygen consumption rate tester
CN105928846B (en) A kind of measuring system and its measuring method of aerosol scattering moisture absorption growth factor
CN209196229U (en) A kind of wet device of new gas control oxygen control
CN201241970Y (en) Gas three-way regulating valve
CN101655413A (en) Testing device for quickly detecting flow property parameters of air passage of internal combustion engine
CN102297163A (en) Water pumping device and method for U-shaped channel
CN110132804A (en) A kind of nanometer aerosol hygroscopicity measuring system and method
CN107096371A (en) The lime stone slurry supply system and adjusting method of a kind of wide Load Regulation
CN107194046B (en) Dimension analysis-based aerator performance prediction method
CN204346803U (en) For the controllable pressure of gaseous sample and the dynamic dilution device of humidity
CN202974749U (en) Gas distributing device for simulating alcohol content of exhaled air by saturated vapor method
CN111408243B (en) Wet desulfurization pH value control system and method for thermal power generating unit
CN102297164A (en) Multi-pipe wheel-free pump
CN112859974A (en) Cooling tower water supplement control system based on environmental meteorological parameters and unit operation parameters
CN112965562A (en) Humidity control structure and control method of temperature and humidity verification box
CN105617898A (en) CO2 mixed gas preparing device
CN110314526A (en) A kind of serum recycle system adjusts space calculation method and its device
CN202690025U (en) One-dimensional fireflood physical simulation device
CN207335029U (en) A kind of humidification system
CN110898637A (en) Preparation process of coal-fired boiler flue gas desulfurization efficiency calculation method
CN202402018U (en) Wet steam distributor
CN113919177A (en) Energy-saving potential evaluation method and system suitable for wet desulphurization system of coal-fired power plant

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant