CN106621883A - Portable type multi-component gas diluting device - Google Patents

Portable type multi-component gas diluting device Download PDF

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Publication number
CN106621883A
CN106621883A CN201611232749.4A CN201611232749A CN106621883A CN 106621883 A CN106621883 A CN 106621883A CN 201611232749 A CN201611232749 A CN 201611232749A CN 106621883 A CN106621883 A CN 106621883A
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CN
China
Prior art keywords
pipeline
diluted
gas
connector
bit triplet
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Pending
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CN201611232749.4A
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Chinese (zh)
Inventor
张晓燕
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Individual
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Individual
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Priority to CN201611232749.4A priority Critical patent/CN106621883A/en
Publication of CN106621883A publication Critical patent/CN106621883A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/10Mixing gases with gases
    • B01F23/19Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20Measuring; Control or regulation
    • B01F35/21Measuring
    • B01F35/211Measuring of the operational parameters
    • B01F35/2114Speed of feeding material, e.g. bands or strips
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20Measuring; Control or regulation
    • B01F35/22Control or regulation
    • B01F35/221Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
    • B01F35/2213Pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20Measuring; Control or regulation
    • B01F35/22Control or regulation
    • B01F35/221Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
    • B01F35/2214Speed during the operation
    • B01F35/22141Speed of feeding of at least one component to be mixed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20Measuring; Control or regulation
    • B01F35/22Control or regulation
    • B01F35/221Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
    • B01F35/2215Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/25Mixing waste with other ingredients

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

The invention provides a portable type multi-component gas diluting device. The portable type multi-component gas diluting device comprises a diluting pipeline, a first to-be-diluted pipeline and a second to-be-diluted pipeline, wherein the diluting pipeline is used for conveying diluting gas; the first to-be-diluted pipeline is used for conveying first to-be-diluted gas; the second to-be-diluted pipeline is used for conveying second to-be-diluted gas; the first to-be-diluted pipeline, the second to-be-diluted pipeline and the diluting pipeline are communicated by a tee valve, and the flows of the first to-be-diluted pipeline, second to-be-diluted pipeline and diluting pipeline are collected onto an exit pipeline after passing through a mass flowmeter, and discharged through a standard gas outlet. The portable type multi-component gas diluting device has the advantages that by arranging multiple to-be-diluted pipelines and diluting gas, multiple types of gases with target concentrations can be prepared simultaneously; the multi-component gas can be simultaneously prepared, and the study problem of crossing interference of gas in the smoke detection field is solved.

Description

A kind of portable multicomponent gases air mix facilities
Technical field
The invention belongs to environmental protecting device technical field, specifically, the present invention relates to a kind of portable multicomponent gases are dilute Release device, for there is certain concentration one-component or multicomponent mixed gas device in places such as polluter scene, laboratorys, especially It is applied to using High Purity Nitrogen or pure air as point gas dilution of background gas.
Background technology
Can be using normal concentration gas to monitoring device or system linearity, drift in the management of discharge of pollutant sources waste gas monitoring The performance parameters such as shifting, accuracy carry out test Management of quality control, and the existing gas of normal concentration under normal circumstances all adopts steel cylinder gas, and With the progressively popularization that generating set minimum discharge is transformed, polluter is particularly coal-burning power plant's exhaust gas concentration and is down to ultralow limit value, Such as SO2:35mg/Nm3、NOx:50mg/Nm3.Scene is accomplished by the calibrating gas of low concentration and carries out Quality Control pipe to minimum discharge system Reason, and configure bottled light concentration gas and there are problems that big preparation difficulty, high cost, stability are poor and live. If using portable gas air mix facilities, you can need to configure variable concentrations gas according to scene, scene is met different dense The demand of degree Standard Gases.
Realized using two-way mass flow controller more than existing standard gas dilution device, principle is using high-purity all the way Nitrogen or compressed air carry out dilution proportion for background gas to high concentrations of gas known to another road, obtain certain concentration gas.It is such Gas dilution device has that single function, poor anti jamming capability, portability are poor, precision is low for configuration, effusion meter drift is big, operation not Just the problems such as.
Accordingly, it is desirable to provide a kind of improved technology scheme not enough for above-mentioned prior art.
The content of the invention
It is an object of the invention to provide a kind of portable multicomponent gases air mix facilities, at least to solve in prior art The technical problem of the portable performance difference that calibrating gas air mix facilities is present, operate not present in prior art while can solve the problem that Just technical problem.
In order to solve the above problems, the present invention provides a kind of portable multicomponent gases air mix facilities, and its technical scheme is such as Under:
A kind of portable multicomponent gases air mix facilities, including dilution pipeline, for conveying diluent gas;First is to be diluted Pipeline, for conveying the first gas to be diluted;Second pipeline to be diluted, for conveying the second gas to be diluted;Described first Pipeline to be diluted is provided with the second two-bit triplet electromagnetic valve, and the first connector of the second two-bit triplet electromagnetic valve and second connect Interface is both connected on the described first pipeline to be diluted;The 3rd two-bit triplet electromagnetism is provided with the described second pipeline to be diluted Valve, first connector and the second connector of the 3rd two-bit triplet electromagnetic valve are both connected to the described second pipeline to be diluted On;Diversion three-way valve is provided with the dilution pipeline, first connector and the second connector of the diversion three-way valve connect It is connected on the dilution pipeline, the 3rd connector of the diversion three-way valve is connected to described 3rd two three by tie point On 3rd connector of three-way electromagnetic valve;The three-way valve that confluxes, the first company of the three-way valve that confluxes are provided with the tie point Interface and the second connector are both connected in the tie point, and the 3rd connector of the three-way valve that confluxes passes through the second branch road It is connected on the 3rd connector of the second two-bit triplet electromagnetic valve;The first mass flow is provided with the dilution pipeline Meter, on the described first pipeline to be diluted the second mass flowmenter is provided with, and on the described second pipeline to be diluted the 3rd matter is provided with Amount effusion meter;The tail end of the dilution pipeline, first pipeline to be diluted and second pipeline to be diluted confluxes in outlet Exported by Standard Gases outlet on pipeline.
Portable multicomponent gases air mix facilities described above, more preferably:Also include deep cooling heated for controlling temperature constant temperature Box, to first mass flowmenter, second mass flowmenter and the 3rd mass flowmenter thermostatic control is carried out.
Portable multicomponent gases air mix facilities described above, more preferably:Also include air pipe line;It is air-dried Device, installed in the head end of the air pipe line;Filter, on the air pipe line and positioned at described dress is air-dried The rear put;High pressure air pump, on the air pipe line and positioned at the rear of the filter;With the first two-bit triplet Electromagnetic valve, on the dilution pipeline, first connector and the second connector of the first two-bit triplet electromagnetic valve is equal It is connected on the dilution pipeline, the tail end of the air pipe line is connected to the 3rd connection of the first two-bit triplet electromagnetic valve On mouth.
Portable multicomponent gases air mix facilities described above, more preferably:The first two-bit triplet electromagnetic valve Positioned at the front of the diversion three-way valve.
Portable multicomponent gases air mix facilities described above, more preferably:Also include normal flow generating meanss, It is connected with first mass flowmenter, second mass flowmenter and the 3rd mass flowmenter respectively, for realizing The calibration of first mass flowmenter, second mass flowmenter and the 3rd mass flowmenter.
Portable multicomponent gases air mix facilities described above, more preferably:Also include gas mixing device, installed in institute State on export pipeline, for gas mixing is uniform.
Portable multicomponent gases air mix facilities described above, more preferably:The gas mixing device is the remittance of strong flow-disturbing Stream tank.
Portable multicomponent gases air mix facilities described above, more preferably:The strong flow-disturbing confluxes tank including tank Body, for providing receiving space;Air inlet pipe, the lower sidewall position on front side of the tank body;Escape pipe, positioned at the tank body The side wall upper part position of rear side;First spoiler, in the tank body, before the antetheca and tank body of first spoiler Side inwall laminating, formed gas passage between the rear wall of first spoiler and the rear side inwall of tank body, gas is disturbed by first Gas passage of crossing between stream plate and tank body is flowed up;With the second spoiler, in the tank body and be located at described first The top of spoiler, the rear wall of the second spoiler is fitted with the rear side inwall of tank body, before the antetheca and tank body of the second spoiler Gas passage was formed between the inwall of side, gas is flowed up by the gas passage of crossing between the second spoiler and tank body.
Portable multicomponent gases air mix facilities described above, more preferably:Also include the first pressure regulator valve, be arranged on On the dilution pipeline, and positioned at the front of the first two-bit triplet electromagnetic valve, for pressure regulation;Second pressure regulator valve, is arranged on On first pipeline to be diluted, and positioned at the front of the second two-bit triplet electromagnetic valve, for pressure regulation;3rd pressure regulator valve, It is arranged on the described second pipeline to be diluted, and positioned at the front of the 3rd two-bit triplet electromagnetic valve, for pressure regulation.
Portable multicomponent gases air mix facilities described above, more preferably:Also include constant pressure before first flowmeter Device, is arranged on the dilution pipeline, and positioned at the front of first mass flowmenter;Constant pressure dress before second flowmeter Put, be arranged on the described first pipeline to be diluted, and positioned at the front of second mass flowmenter;Constant pressure before 3rd effusion meter Device, is arranged on the described second pipeline to be diluted, and positioned at the front of the 3rd mass flowmenter.
Analysis understands that compared with prior art, the advantages of the present invention are:The present invention has integrated level Height, compact conformation, small volume and advantage easy to carry.The deep cooling heated for controlling temperature constant temp. box that the present invention is adopted has high-accuracy and constant Warm control function, it is to avoid impact of the electric circuit temperature drift to distribution precision;Intelligence degree is high, using industry control flat board as master control Device, degree of stability is high;There is normal concentration in achievable multicomponent, solve the research puzzle of multicomponent cross interference simultaneously;Carry height Pressure air pump is taken as pump, can purge as carrier gas background gas and full-range anticorrosion from pure air is produced, existing Field strong adaptability.Multimass effusion meter coordinates the distribution for being also capable of achieving one-component width thinner ratio.
Description of the drawings
Fig. 1 is the block schematic illustration of the portable multicomponent gases air mix facilities of the preferred embodiment of the present invention;
Fig. 2 confluxes the structural representation of tank for the strong flow-disturbing of the preferred embodiment of the present invention;
Fig. 3 is the top view of Fig. 2;
Fig. 4 is the block schematic illustration of the shell of the preferred embodiments of the present invention;
In figure:1- diluent gas;The gases to be diluted of 2- first;The gases to be diluted of 3- second;The pressure regulator valves of 41- first;42- Two pressure regulator valves;The pressure regulator valves of 43- the 3rd;51- the first two-bit triplet electromagnetic valves;52- the second two-bit triplet electromagnetic valves;The 3rd liang of 53- Position-3-way solenoid valve;6- confluxes three-way valve;7- diversion three-way valves;The mass flowmenters of 81- first;The mass flowmenters of 82- second; The mass flowmenters of 83- the 3rd;Constant voltage equipment before 91- first flowmeters;Constant voltage equipment before 91- second flowmeters;The flows of 93- the 3rd Constant voltage equipment before meter;The strong flow-disturbings of 10- conflux tank;101- air inlet pipe;102- escape pipes;The spoilers of 103- first;104- second is disturbed Stream plate;11- outlet constant voltage equipments;12- air dry-sets;13- filters;14- high pressure air pumps;15- deep cooling heated for controlling temperature Constant temp. box;16- Standard Gases are exported;17- shells.
Specific embodiment
The present invention is described in further details with reference to the accompanying drawings and detailed description.It should be noted that not In the case of conflict, the embodiment and the feature in embodiment in the present invention can be mutually combined.
In describing the invention, term " longitudinal direction ", " horizontal ", " on ", it is D score, "front", "rear", "left", "right", " perpendicular Directly ", the orientation or position relationship of the instruction such as " level ", " top ", " bottom " is, based on orientation shown in the drawings or position relationship, to be only For the ease of describing the present invention rather than requiring that the present invention must be with specific azimuth configuration and operation therefore it is not intended that right The restriction of the present invention.Term " connected " used in the present invention, " connection " should be interpreted broadly, for example, it may be fixedly connected, Can also be detachably connected;Can be joined directly together, it is also possible to be indirectly connected to by intermediate member, it is common for this area For technical staff, the concrete meaning of above-mentioned term can be as the case may be understood.
As shown in Figure 1, Figure 2 and Figure 3, the portable multicomponent gases air mix facilities of the preferred embodiment of the present invention mainly includes Dilution pipeline (not shown), for conveying diluent gas 1;First pipeline (not shown) to be diluted is to be diluted for conveying first Gas 2;Second pipeline (not shown) to be diluted, for conveying the second gas to be diluted 3;Is provided with the first pipeline to be diluted Two two-bit triplet electromagnetic valves 52, first connector and the second connector of the second two-bit triplet electromagnetic valve 52 are both connected to first and treat On dilution pipeline;The 3rd two-bit triplet electromagnetic valve 53 is provided with the second pipeline to be diluted, the 3rd two-bit triplet electromagnetic valve 53 First connector and the second connector are both connected on the second pipeline to be diluted;Diversion three-way valve 7 is provided with dilution pipeline, point First connector and the second connector of stream three-way valve 7 is both connected to dilute on pipeline, and the 3rd connector of diversion three-way valve 7 leads to Cross tie point to be connected on the 3rd connector of the 3rd two-bit triplet electromagnetic valve 53;The three-way valve that confluxes is provided with the first leg 6, first connector and the second connector of the three-way valve 6 that confluxes are all connected with the first leg, the 3rd connection of the three-way valve 6 that confluxes Mouth is connected on the 3rd connector of the second two-bit triplet electromagnetic valve 52 by the second branch road;The first matter is provided with dilution pipeline Amount effusion meter 81, is provided with the second mass flowmenter 82 on the first pipeline to be diluted, and on the second pipeline to be diluted the 3rd is provided with Mass flowmenter 83;The tail end of dilution pipeline, the first pipeline to be diluted and the second pipeline to be diluted confluxes and leads on export pipeline Cross Standard Gases outlet 16 to export.
Sum it up, the portable multicomponent gases air mix facilities that provides of the present invention by arrange multichannel pipeline to be diluted and Diluent gas, such as the first gas to be diluted 2 are sulfur dioxide, and the second gas to be diluted 3 is nitric oxide, the 3rd gas to be diluted For other, diluent gas 1 is that High Purity Nitrogen or startup sampling are pumped into air;So can simultaneously configure plurality of target concentration gas Body;And multicomponent gases can be simultaneously configured, solve the research puzzle of flue gas inspection field gas cross interference;Furthermore this Conflux three-way valve 6 and the diversion three-way valve 7 of bright setting combines diluent gas 1 when being air, can be by air to the first mass Effusion meter 81, the second mass flowmenter 82 and the 3rd mass flowmenter 83 are purged and calibrated;Again can be to the first pipe to be diluted Road and the second pipeline to be diluted are cleared up.
In order to make mass flowmenter in Suitable ranges, as shown in figure 1, present invention additionally comprises deep cooling adds thermal control Warm constant temp. box 15, to the first mass flowmenter 81, the second mass flowmenter 82 and the 3rd mass flowmenter 83 and control circuit portion Dividing carries out thermostatic control.In the present invention, the first mass flowmenter 81, the second mass flowmenter 82 and the 3rd mass flowmenter 83 Positioned at same vertical position, i.e. the first mass flowmenter 81, the second mass flowmenter 82 and the 3rd mass flowmenter 83 in arranged side by side Arrange and positioned at the same vertical position of differing heights.The present invention adopts deep refrigerating heated for controlling temperature technology, to mass flowmenter And control circuit part adopts narrow thermostatic control, temperature control precision is reduced because of the zones of different temperature difference pair up to 0.1 degree Celsius The temperature drift effects that circuit is caused so that condition is consistent when calibration when mass flowmenter works, solve temperature drift Move the impact to distribution precision.
The present invention is using digital communication mode to the first mass flowmenter 81, the second mass flowmenter 82 and the 3rd quality stream Gauge 83 carries out flow set and closed loop feedback flow monitoring;With control accuracy is higher, stability is higher, response is faster Feature, at the scene anti-interference type is higher for digital communication mode, may be implemented in long-time under the conditions of industry spot complexity electromagnetic interference Stable distribution;In the present invention, selection is ground Chinese workers' control flat board and carries out digital communication.
The present invention using pure air as diluent gas, or can utilize pure air sometimes in dilution Purging function is carried out to the full gas circuit of the present invention, based on this, as shown in figure 1, present invention additionally comprises air pipe line (not shown), empty Gas drying device 12, installed in the head end of air pipe line;Filter 13, on air pipe line and positioned at air dry-set 12 rear;High pressure air pump 14, on air pipe line and positioned at the rear of filter 13;With the first two-bit triplet electromagnetism Valve 51, on dilution pipeline, first connector and the second connector of the first two-bit triplet electromagnetic valve 51 are both connected to dilute Release on pipeline, the tail end of air pipe line is connected on the 3rd connector of the first two-bit triplet electromagnetic valve 51.Preferably first liang Position-3-way solenoid valve 51 is located at the front of diversion three-way valve 7.Present invention configuration high pressure air pump 14, makees using pure air Distribution dilution or full gas circuit purging function are carried out for background gas, 1. because diluent gas is mainly with High Purity Nitrogen as background gas, is consumed Amount is huge, and background gas can be used air as in the case where Oxygen Condition is not considered to dilute aimed concn gas;2. it is often during distribution Using high standard gas such as SO2, NO etc., all with certain corrosion type, the present invention is by the first two-bit triplet electromagnetic valve 51 The front of diversion three-way valve 7 is arranged on, whole process pure air purging function can be carried out using after terminating in the present invention, kept away Exempt from residual gas and corrosion damage is caused to mass flowmenter and each pipeline.
In the present invention, also including normal flow generating meanss (not shown), respectively with the first mass flowmenter 81, second Mass flowmenter 82 is connected with the 3rd mass flowmenter 83, for realizing the first mass flowmenter 81, the second mass flowmenter 82 With the calibration of the 3rd mass flowmenter 83.Mass flow controller software calibration function is realized, in hardware not side is directly calibrated When just, can be combined with software using normal flow generating meanss and be calibrated.
The mixed gas of Quick uniform under in order to realize different flow, it is ensured that the Standard Gases even concentration of generation, such as Fig. 1 institutes Show, present invention additionally comprises gas mixing device, on export pipeline, for gas mixing is uniform.As shown in figure 1, of the invention Gas mixing device conflux tank 10 for strong flow-disturbing.As shown in Figures 2 and 3, preferably, strong flow-disturbing confluxes tank 10 including tank body, is used for Receiving space is provided;Air inlet pipe 101, the lower sidewall position on front side of tank body;Escape pipe 102, the side on rear side of tank body Wall upper position;First spoiler 103, in tank body, the antetheca of the first spoiler 103 is pasted with the front inner wall of tank body Close, formed gas passage between the rear wall of the first spoiler 103 and the rear side inwall of tank body, gas by the first spoiler 103 with Gas passage of crossing between tank body is flowed up;With the second spoiler 104, in tank body and first spoiler 103 is located at Top, the rear wall of the second spoiler 104 is fitted with the rear side inwall of tank body, the antetheca of the second spoiler 104 and the front side of tank body Gas passage was formed between inwall, gas is flowed up by the gas passage of crossing between the second spoiler 104 and tank body.In the present invention In, air inlet pipe 101 is located at bottom, is up followed successively by the first spoiler 103, the second spoiler 104 and gas outlet 102.In order to Uniform effect can be further functioned as, between the straight line and the centrage of tank body at the place of air inlet pipe 101 of the present invention folder is formed Angle, the angle of preferred angle is 45 °;Formed between the straight line and the centrage of tank body at escape pipe 102 of the invention place in the same manner Angle, the angle of preferred angle is 45 °.The gas mixing device inside of the present invention is designed using strong turbulence structure, is capable of achieving not cocurrent flow The mixed gas of the lower Quick uniform of amount, it is ensured that the Standard Gases even concentration of generation.
For the ease of the Stress control to diluent gas 1, as shown in figure 1, present invention additionally comprises the first pressure regulator valve 41, is arranged On dilution pipeline, and positioned at the front of the first two-bit triplet electromagnetic valve 51, for pressure regulation.In the same manner, present invention additionally comprises second Pressure regulator valve 42, is arranged on the first pipeline to be diluted, and positioned at the front of the second two-bit triplet electromagnetic valve 52, for pressure regulation.This Invention also includes the 3rd pressure regulator valve 43, is arranged on the second pipeline to be diluted, and before the 3rd two-bit triplet electromagnetic valve 53 Side, for pressure regulation.
Diluent gas 1 enter the first mass flowmenter 81 before, need to carry out constant pressure to diluent gas 1, based on this, such as Shown in Fig. 1, present invention additionally comprises constant voltage equipment 91 before first flowmeter, are arranged on dilution pipeline, and positioned at the first quality stream The front of gauge 81.In concrete setting, constant voltage equipment 91 is located at the rear of diversion three-way valve 7 before first flowmeter.In the same manner, this It is bright also to include constant voltage equipment 92 before second flowmeter, it is arranged on the first pipeline to be diluted, and positioned at the second mass flowmenter 82 Front.Present invention additionally comprises constant voltage equipment 93 before the 3rd effusion meter, is arranged on the second pipeline to be diluted, and positioned at the 3rd matter The front of amount effusion meter 83.
In order to guarantee the gas after diluting in voltage stabilizing state, as shown in figure 1, present invention additionally comprises outlet constant pressure dress 11 are put, is arranged on export pipeline, and positioned at the rear of gas mixing device.
What the present invention was arranged conflux three-way valve 6 and diversion three-way valve 7 can be realized being passed through the two-way mass flowmenter of gas Configuration is used, it is ensured that the distribution precision of carrier gas.
In practice, the mass flowmenter of the present invention adopts Sevenstar-HC CS100 Series Digital mass flowmenters, It is that 500ml/min, C are 2L/min that range is respectively A for 2L/min, B, according to thinner ratio in flow restriction, this time dilution computing In relate only to 2L/min High Purity Nitrogens and participate in dilution with the sulfur dioxide on the tunnels of 500ml/min mono- all the way;It is highly concentrated that the present invention is used Degree calibrating gas are 6000mg/M3Sulfur dioxide, background gas are High Purity Nitrogen (99.999%);Configuration flow is 1L/min, concentration For 200mg/M3、100mg/M3、50mg/M3、25mg/M3;Thermostatic control is at 25 DEG C ± 0.1 DEG C;Close using Jiangsu metering universities and colleges are accurate Instrument is used as datum mark after lattice.
As shown in figure 4, present invention additionally comprises shell 17, for accommodating pressure regulator valve, two-bit triplet electromagnetic valve, threeway of confluxing Before valve, diversion three-way valve, mass flowmenter, effusion meter constant voltage equipment, strong flow-disturbing conflux tank, outlet constant voltage equipment, be air-dried Device, filter, high pressure air pump, deep cooling heated for controlling temperature constant temp. box;The present invention is provided with carrying handle (not on the top of shell 17 Diagram).The present invention is accommodated miscellaneous part in it by shell 17, makes the present invention have compact conformation, small volume and carrying side Just the characteristics of.
Analysis understands that compared with prior art, the advantages of the present invention are:The present invention has integrated level Height, compact conformation, small volume and advantage easy to carry.The deep cooling heated for controlling temperature constant temp. box 15 that the present invention is adopted has high accuracy Thermostatic control function, it is to avoid impact of the electric circuit temperature drift to distribution precision;Intelligence degree is high, using industry control flat board as master control Device, degree of stability is high;There is normal concentration in achievable multicomponent, solve the research puzzle of multicomponent cross interference simultaneously;Carry height Pressure air pump 14 is taken as pump, can purge as carrier gas background gas and full-range anticorrosion from pure air is produced, Live strong adaptability.Multimass effusion meter coordinates the distribution for being also capable of achieving one-component width thinner ratio.
As known by the technical knowledge, the present invention can be by other essence without departing from its spirit or the embodiment party of essential feature Case is realizing.Therefore, embodiment disclosed above, for each side, is all merely illustrative, and is not only.Institute Have and be included in the invention within the scope of the present invention or in the change being equal in the scope of the present invention.

Claims (10)

1. a kind of portable multicomponent gases air mix facilities, it is characterised in that include:
Dilution pipeline, for conveying diluent gas;
First pipeline to be diluted, for conveying the first gas to be diluted;
Second pipeline to be diluted, for conveying the second gas to be diluted;
It is provided with the second two-bit triplet electromagnetic valve on the described first pipeline to be diluted, the first of the second two-bit triplet electromagnetic valve Connector and the second connector are both connected on the described first pipeline to be diluted;The 3rd is provided with the described second pipeline to be diluted Two-bit triplet electromagnetic valve, first connector and the second connector of the 3rd two-bit triplet electromagnetic valve are both connected to described second On pipeline to be diluted;Diversion three-way valve, first connector and second of the diversion three-way valve are provided with the dilution pipeline Connector is both connected on the dilution pipeline, and the 3rd connector of the diversion three-way valve is connected to described by tie point On 3rd connector of the 3rd two-bit triplet electromagnetic valve;The three-way valve that confluxes, the threeway of confluxing are provided with the tie point First connector and the second connector of valve is both connected in the tie point, and the 3rd connector of the three-way valve that confluxes leads to Cross the second branch road to be connected on the 3rd connector of the second two-bit triplet electromagnetic valve;First is provided with the dilution pipeline Mass flowmenter, on the described first pipeline to be diluted the second mass flowmenter is provided with, and is set on the described second pipeline to be diluted There is the 3rd mass flowmenter;The tail end of the dilution pipeline, first pipeline to be diluted and second pipeline to be diluted converges Stream is exported on export pipeline by Standard Gases outlet.
2. portable multicomponent gases air mix facilities according to claim 1, it is characterised in that also include:
Deep cooling heated for controlling temperature constant temp. box, to first mass flowmenter, second mass flowmenter and the 3rd mass Effusion meter carries out thermostatic control.
3. portable multicomponent gases air mix facilities according to claim 1, it is characterised in that also include:
Air pipe line;
Air dry-set, installed in the head end of the air pipe line;
Filter, on the air pipe line and positioned at the rear of the air dry-set;
High pressure air pump, on the air pipe line and positioned at the rear of the filter;With
First two-bit triplet electromagnetic valve, on the dilution pipeline, the first connection of the first two-bit triplet electromagnetic valve Mouth and the second connector are both connected on the dilution pipeline, and the tail end of the air pipe line is connected to first two-bit triplet On 3rd connector of electromagnetic valve.
4. portable multicomponent gases air mix facilities according to claim 3, it is characterised in that:
The first two-bit triplet electromagnetic valve is located at the front of the diversion three-way valve.
5. portable multicomponent gases air mix facilities according to claim 1, it is characterised in that also include:
Normal flow generating meanss, respectively with first mass flowmenter, second mass flowmenter and the 3rd matter Amount effusion meter is connected, for realizing first mass flowmenter, second mass flowmenter and the 3rd mass flow The calibration of meter.
6. portable multicomponent gases air mix facilities according to claim 1, it is characterised in that also include:
Gas mixing device, on the export pipeline, for gas mixing is uniform.
7. portable multicomponent gases air mix facilities according to claim 6, it is characterised in that:
The gas mixing device confluxes tank for strong flow-disturbing.
8. portable multicomponent gases air mix facilities according to claim 7, it is characterised in that the strong flow-disturbing confluxes tank Including:
Tank body, for providing receiving space;
Air inlet pipe, the lower sidewall position on front side of the tank body;
Escape pipe, the side wall upper part position on rear side of the tank body;
First spoiler, in the tank body, the antetheca of the first spoiler is fitted with the front inner wall of tank body, described Gas passage was formed between the rear wall of the first spoiler and the rear side inwall of tank body, gas is by between the first spoiler and tank body Cross gas passage to flow up;With
Second spoiler, in the tank body and be located at first spoiler top, the rear wall of the second spoiler with The rear side inwall laminating of tank body, formed gas passage between the antetheca of the second spoiler and the front inner wall of tank body, gas is by the Gas passage of crossing between two spoilers and tank body is flowed up.
9. portable multicomponent gases air mix facilities according to claim 3, it is characterised in that also include:
First pressure regulator valve, is arranged on the dilution pipeline, and positioned at the front of the first two-bit triplet electromagnetic valve, for adjusting Pressure;
Second pressure regulator valve, is arranged on the described first pipeline to be diluted, and positioned at the front of the second two-bit triplet electromagnetic valve, For pressure regulation;
3rd pressure regulator valve, is arranged on the described second pipeline to be diluted, and positioned at the front of the 3rd two-bit triplet electromagnetic valve, For pressure regulation.
10. portable multicomponent gases air mix facilities according to claim 1, it is characterised in that also include:
Constant voltage equipment before first flowmeter, is arranged on the dilution pipeline, and positioned at the front of first mass flowmenter;
Constant voltage equipment before second flowmeter, is arranged on the described first pipeline to be diluted, and positioned at second mass flowmenter Front;
Constant voltage equipment before 3rd effusion meter, is arranged on the described second pipeline to be diluted, and positioned at the 3rd mass flowmenter Front.
CN201611232749.4A 2016-12-28 2016-12-28 Portable type multi-component gas diluting device Pending CN106621883A (en)

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CN108097138A (en) * 2017-11-29 2018-06-01 中国海洋石油集团有限公司 Light hydrocarbons measured portions mixing arrangement
CN108225855A (en) * 2018-01-17 2018-06-29 环境保护部华南环境科学研究所 One kind can temperature control combustion chamber and flue gas dilution sampling system
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CN114486470A (en) * 2021-12-31 2022-05-13 南京理工大学 Multi-path gas smoke generation and scattering integrated device

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CN114486470A (en) * 2021-12-31 2022-05-13 南京理工大学 Multi-path gas smoke generation and scattering integrated device

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Application publication date: 20170510