CN106093301A - Standard Gases generation control method, system and standard gas distribution meter under a kind of operating mode - Google Patents
Standard Gases generation control method, system and standard gas distribution meter under a kind of operating mode Download PDFInfo
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- CN106093301A CN106093301A CN201610394632.XA CN201610394632A CN106093301A CN 106093301 A CN106093301 A CN 106093301A CN 201610394632 A CN201610394632 A CN 201610394632A CN 106093301 A CN106093301 A CN 106093301A
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- reagent
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- gasification
- volume
- generation control
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- 239000007789 gas Substances 0.000 title claims abstract description 127
- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 95
- 238000002309 gasification Methods 0.000 claims abstract description 62
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000012937 correction Methods 0.000 claims abstract description 11
- 230000002572 peristaltic effect Effects 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000004868 gas analysis Methods 0.000 abstract description 11
- 239000010813 municipal solid waste Substances 0.000 description 7
- 238000001514 detection method Methods 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 239000012159 carrier gas Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 229940124597 therapeutic agent Drugs 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 238000004056 waste incineration Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000009790 rate-determining step (RDS) Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0009—General constructional details of gas analysers, e.g. portable test equipment
- G01N33/007—Arrangements to check the analyser
-
- G01N33/0072—
Abstract
This application discloses a kind of Standard Gases generation control method, system and standard gas distribution meter, this control method and system are applied to standard gas distribution meter, it is specially the reagent volume of the reagent obtained in the heating and gasifying mixing bunker being transported to standard gas distribution meter, utilize temperature sensor to obtain the working temperature under current working simultaneously, then utilize default ideal gas formula that working temperature is calculated, obtain revising gasification coefficient, finally utilize correction gasification coefficient that reagent volume is calculated, obtain the actual volume of the reagent gas after reagent gasifies under current working.Owing to the generation control method that the application provides have references to the working temperature of current working, so that to reagent gasification after the volume of reagent gas tally with the actual situation, deviation is not had with the volumetric quantities of reality, the concentration value the most just making standard gas distribution meter reality is consistent with reagent concentration such that it is able to avoid producing error when calibrating gas analysis system.
Description
Technical field
The application relates to environmental technology field, more particularly, it relates to Standard Gases generation control method under a kind of operating mode, be
System and standard gas distribution meter.
Background technology
In China, " National urban domestic garbage was harmlessly treated Facilities Construction Eleventh Five-Year Plan " is pointed out, sends out in economy
Reach, MSW heating value is eligible, the city of shortage of land resource, can add great development incineration treatment technology；New Zengcheng City is raw
Installation for rubbish processing to be harmless 479 alive, wherein garbage burning factory 82, account for 17.1%, the day of average single seat incineration plant processes
Ability is about 810 tons.And the Eleventh Five-Year Plan period, plan domestic waste harmless treatment rate reaches 70%, urban life
Installation for rubbish processing to be harmless construction plan gross investment is 58,900,000,000 yuan, and the gross investment of Tenth Five-Year Plan Period is 19,800,000,000 yuan, contrast
Can be seen that, the increase volumn of investment in China's domestic waste harmless treatment Facilities Construction is obviously.
Waste incineration and generating electricity belongs to the biomass power generation in the middle of renewable energy power generation, according to " renewable energy power generation valency
Lattice and expense allocation management trial method " (send out change price [2006] 7) biomass power generation electricity price standard by each province (autonomous region,
Municipality directly under the Central Government) desulfurization coal unit mark post rate for incorporation into the power network added subsidy electricity price composition 2005 years, and subsidy electricity price standard is every kilowatt hour
0.25 yuan.Country also takes multinomial preferential policy to be protected for garbage power simultaneously: one is that generated energy is all purchased；Two are
Eliminate the collection of value-added tax, and on income tax, enjoy deduction and exemption policy；Three be country can by garbage disposal subsidy in the way of to
Corporate payments service charge, the most so-called refuse disposal expense.
Support energetically based on above national policy, we will be it is believed that China's incineration treatment of garbage ratio will continue
Steadily improve, within 2010, be expected to reach 18%.In conjunction with the developing state that market is current, following one period, use the sides such as BOT
Formula is built incineration plant and will progressively be occupied leading, the golden period burning development by welcoming China in 2008～2015.
It is exactly environmental protection problem that waste incineration project relates to national most concerned thing, and a large amount of flue gases enter air,
The annual pollution number causing air is in terms of ten thousand tons.This is accomplished by waste incineration station is carried out process control, utilizes gas analysis
System is the key point of this process control to the most up to standard detection of flue gas of discharge.
In order to enable gas analysis system normally to work, need to utilize standard gas distribution meter to export unconventional standard
Gas, to calibrate gas analysis system.Standard gas distribution meter is made up of gas circuit and fluid path two parts, gas circuit as carrier gas,
By mass flow controller quantified controlling；Fluid path part includes high Accuracy Electronic Balance and peristaltic pump control system；Distribution process
For: the vaporizing liquid of constant current speed and quantitative carrier gas are mixed to get the Standard Gases of any concentration by peristaltic pump, and reagent can be water, has
Machine reagent, inorganic reagent (Hcl, HF, NH3, Hgcl2 etc.).
Needing the Standard Gases obtaining certain concentration when, standard gas distribution meter needs to determine the gasification of certain volume
Reagent obtains after mixing with the carrier gas of certain volume, due to standard gas distribution meter the timing signal that dispatches from the factory be standard conditions,
Generally demarcate under the conditions of mark condition, and the working temperature of Workplace and this standard temperature typically can deviation, cause
The volume of the reagent gas produced under working condition and the volumetric quantities deviation of display, this can cause the concentration value of display
There is bigger error with the actual concentrations of Standard Gases, and then can make when utilizing this Standard Gases that gas analysis system is calibrated
Become certain error.
Summary of the invention
In view of this, the application provides Standard Gases generation control method, system and standard gas distribution meter under a kind of operating mode, with
Avoid causing error when utilizing this Standard Gases that gas analysis system is calibrated.
To achieve these goals, it is proposed that scheme as follows:
Standard Gases generation control method under a kind of operating mode, is applied to standard gas distribution meter, comprises the steps:
Acquisition is transported to the reagent volume of the reagent in the heating and gasifying mixing bunker of described standard gas distribution meter；
Temperature sensor is utilized to obtain the working temperature under current working；
Utilize the ideal gas formula preset that described working temperature is calculated, obtain revising gasification coefficient；
Utilize described gasification coefficient of revising that described reagent volume is calculated, obtain described reagent gasification under current working
After the actual volume of reagent gas.
Optionally, the reagent of the reagent in described acquisition is transported to the heating and gasifying mixing bunker of described standard gas distribution meter
Volume, including:
Obtain the reagent volume of the reagent of the peristaltic pump output of described standard gas distribution meter.
Optionally, described working temperature is calculated by the ideal gas formula that described utilization is preset, and obtains revising gasification
Coefficient, including:
It is added described 298.15 with described working temperature, obtains both sums；
By 298.15 divided by described and, obtain corrected parameter；
Default gasification constant is multiplied by described corrected parameter, obtains described correction gasification coefficient.
Optionally, described gasification constant is 1244.
Optionally, further comprise the steps of:
Output reflects the actual volume value of described actual volume.
Standard Gases generation control system under a kind of operating mode, is applied to standard gas distribution meter, including:
First acquisition module, the reagent in obtaining the heating and gasifying mixing bunker being transported to described standard gas distribution meter
Reagent volume；
Second acquisition module, for receiving the working temperature under the current working that temperature sensor detects；
First computing module, for utilizing default ideal gas formula to calculate described working temperature, is repaiied
Just gasifying coefficient；
Second computing module, is used for utilizing described gasification coefficient of revising to calculate described reagent volume, obtains current
The actual volume of the reagent gas after described reagent gasifies under operating mode.
Optionally, described second acquisition module is specifically for obtaining the reagent of the peristaltic pump output of described standard gas distribution meter
Reagent volume.
Optionally, described first computing module includes:
Adder unit, for being added described 298.15 with described working temperature, obtains both sums；
Divider, for by 298.15 divided by described and, obtain corrected parameter；
Multiplication unit, for default gasification constant is multiplied by described corrected parameter, obtains described correction gasification coefficient.
Optionally, described gasification constant is 1244.
Optionally, also include:
Output module, for exporting the actual volume value reflecting described actual volume.
A kind of standard gas distribution meter, including Standard Gases generation control system as above.
From above-mentioned technical scheme it can be seen that this application discloses a kind of Standard Gases generation control method, system and mark
Quasi-gas distributing instrument, this control method is applied to standard gas distribution meter, is specially and obtains the heating being transported to standard gas distribution meter
The reagent volume of the reagent in gasification mixing bunker, utilizes temperature sensor to obtain the working temperature under current working, then simultaneously
Utilize the ideal gas formula preset that working temperature is calculated, obtain revising gasification coefficient, finally utilize and revise gasification system
Several reagent volume is calculated, obtain under current working the actual volume of the reagent gas after reagent gasification.Due to the application
The working temperature of current working is provided in the generation control method provided, so that the reagent gas after the reagent gasification arrived
Volume tally with the actual situation, with reality volumetric quantities there is no deviation, the most just make standard gas distribution meter reality concentration value with
Reagent concentration is consistent such that it is able to avoid producing error when calibrating gas analysis system.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present application or technical scheme of the prior art, below will be to embodiment or existing
In having technology to describe, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of application, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to
Other accompanying drawing is obtained according to these accompanying drawings.
The flow chart of steps of a kind of Standard Gases distribution method for generation that Fig. 1 provides for the embodiment of the present application；
The flow chart of steps of a kind of Standard Gases generation control method that Fig. 2 provides for another embodiment of the application；
The structured flowchart of a kind of Standard Gases generation control system that Fig. 3 provides for the another embodiment of the application；
The structured flowchart of a kind of Standard Gases generation control system that Fig. 4 provides for the another embodiment of the application.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present application, the technical scheme in the embodiment of the present application is carried out clear, complete
Describe, it is clear that described embodiment is only some embodiments of the present application rather than whole embodiments wholely.Based on
Embodiment in the application, it is every other that those of ordinary skill in the art are obtained under not making creative work premise
Embodiment, broadly falls into the scope of the application protection.
Embodiment one
The flow chart of steps of a kind of Standard Gases generation control method that Fig. 1 provides for the embodiment of the present application.
As it is shown in figure 1, the Standard Gases generation control method that the present embodiment provides is applied to standard gas distribution meter, Standard Gases is joined
Gas instrument is for output for the Standard Gases calibrating gas analysis system, and concrete control method comprises the steps:
S101: obtain the reagent volume of the reagent being transported in heating vaporization mixing bunker.
I.e. when standard gas distribution meter vaporizes delivery of therapeutic agents in mixing bunker by peristaltic pump to heating, by detection peristaltic pump
Flow determine the volume of reagent, i.e. reagent volume v1 of reagent..
S102: obtain the working temperature of current working.
Temperature sensor is i.e. utilized to obtain the working temperature T under current working1, i.e. the ring of standard gas distribution meter local environment
Border temperature.
S103: utilize ideal gas formula to calculate and revise gasification coefficient.
I.e. utilize default ideal gas formula to above-mentioned working temperature T1Calculate, obtain revising gasification coefficient
k3。
Be specially be added 298.15 with working temperature, obtain with；
Then by 298.15 divided by obtained above and, obtain corrected parameter W.
W=298.15/ (298.15+T1)；
Then default gasification constant k2 is multiplied by this corrected parameter W, obtains revising gasification coefficient k 3, wherein: k3=k2*
298.15/(298.15+T1), wherein gasification constant k2 is 1244.
S104: utilize correction gasification coefficient that reagent volume is calculated.
Gasification coefficient k 3 of revising obtained above is multiplied by reagent volume v1, after obtaining under current working the gasification of this reagent
The actual volume v2 of reagent gas.
Concrete computing formula is: v2=k3*v1
From technique scheme it can be seen that present embodiments provide a kind of Standard Gases generation control method, this controlling party
Method is applied to standard gas distribution meter, the reagent in specially acquisition is transported to the heating and gasifying mixing bunker of standard gas distribution meter
Reagent volume, utilizes temperature sensor to obtain the working temperature under current working simultaneously, then utilizes default preferable gaseous state side
Working temperature is calculated by journey, obtains revising gasification coefficient, finally utilizes correction gasification coefficient to calculate reagent volume,
Obtain the actual volume of the reagent gas after reagent gasifies under current working.Owing to the generation control method that the application provides being joined
According to the working temperature of current working to reagent gasification after the volume of reagent gas tally with the actual situation, with
The volumetric quantities of reality does not has deviation, the most just makes the concentration value of standard gas distribution meter reality be consistent with reagent concentration such that it is able to
Avoid producing error when gas analysis system is calibrated.
Embodiment two
The flow chart of steps of a kind of Standard Gases generation control method that Fig. 2 provides for another embodiment of the application.
As in figure 2 it is shown, the present embodiment is the local correction to a upper embodiment, complete rate-determining steps is as described below:
S201: obtain the reagent volume of the reagent being transported in heating vaporization mixing bunker.
I.e. when standard gas distribution meter vaporizes delivery of therapeutic agents in mixing bunker by peristaltic pump to heating, by detection peristaltic pump
Flow determine the volume of reagent, i.e. reagent volume v1 of reagent..
S202: obtain the working temperature of current working.
Temperature sensor is i.e. utilized to obtain the working temperature T under current working1, i.e. the ring of standard gas distribution meter local environment
Border temperature.
S203: utilize ideal gas formula to calculate and revise gasification coefficient.
I.e. utilize default ideal gas formula to above-mentioned working temperature T1Calculate, obtain revising gasification coefficient
k3。
Be specially be added 298.15 with working temperature, obtain with；
Then by 298.15 divided by obtained above and, obtain corrected parameter W.
W=298.15/ (298.15+T1)；
Then default gasification constant k2 is multiplied by this corrected parameter W, obtains revising gasification coefficient k 3, wherein: k3=k2*
298.15/(298.15+T1), wherein gasification constant k2 is 1244.
S204: utilize correction gasification coefficient that reagent volume is calculated.
Gasification coefficient k 3 of revising obtained above is multiplied by reagent volume v1, after obtaining under current working the gasification of this reagent
The actual volume v2 of reagent gas.
Concrete computing formula is: v2=k3*v1
S205: the actual volume value of output reflection actual volume.
After operator are by the control knob input and output instruction of standard gas distribution meter, by obtained above for instead
The actual volume value reflecting actual volume is exported, and the mode of output can be to print or utilize display device to show,
Thus allow the operator to intuitively obtain this actual volume.
Embodiment three
The structured flowchart of a kind of Standard Gases generation control system that Fig. 3 provides for the another embodiment of the application.
As it is shown in figure 1, the Standard Gases generation control system that the present embodiment provides is joined in standard gas distribution meter, Standard Gases
Gas instrument for the Standard Gases calibrating gas analysis system, specifically includes the first acquisition module, the second acquisition for output
Module, the first computing module and the second computing module.
First acquisition module 10 is for obtaining the reagent volume of the reagent being transported in heating vaporization mixing bunker.
I.e. when standard gas distribution meter vaporizes delivery of therapeutic agents in mixing bunker by peristaltic pump to heating, by detection peristaltic pump
Flow determine the volume of reagent, i.e. reagent volume v1 of reagent..
Second acquisition module 20 is for obtaining the working temperature of current working.
Temperature sensor is i.e. utilized to obtain the working temperature T under current working1, i.e. the ring of standard gas distribution meter local environment
Border temperature.
First computing module 30 is used for utilizing ideal gas formula to calculate and revises gasification coefficient.
I.e. utilize default ideal gas formula to above-mentioned working temperature T1Calculate, obtain revising gasification coefficient
K3, specifically includes adder unit, divider and multiplication unit.
Adder unit for being added 298.15 with working temperature, obtain with；
Divider for by 298.15 divided by obtained above and, obtain corrected parameter W.
W=298.15/ (298.15+T1)；
Multiplication unit, for default gasification constant k2 is multiplied by this corrected parameter W, obtains revising gasification coefficient k 3, its
In: k3=k2*298.15/ (298.15+T1), wherein gasification constant k2 is 1244.
Second computing module 40 is used for utilizing correction gasification coefficient to calculate reagent volume.
Gasification coefficient k 3 of revising obtained above is multiplied by reagent volume v1, after obtaining under current working the gasification of this reagent
The actual volume v2 of reagent gas.
Concrete computing formula is: v2=k3*v1
From technique scheme it can be seen that present embodiments provide a kind of Standard Gases generation control system, this control system
System is applied to standard gas distribution meter, the reagent in specially acquisition is transported to the heating and gasifying mixing bunker of standard gas distribution meter
Reagent volume, utilizes temperature sensor to obtain the working temperature under current working simultaneously, then utilizes default preferable gaseous state side
Working temperature is calculated by journey, obtains revising gasification coefficient, finally utilizes correction gasification coefficient to calculate reagent volume,
Obtain the actual volume of the reagent gas after reagent gasifies under current working.Owing to the generation control method that the application provides being joined
According to the working temperature of current working to reagent gasification after the volume of reagent gas tally with the actual situation, with
The volumetric quantities of reality does not has deviation, the most just makes the concentration value of standard gas distribution meter reality be consistent with reagent concentration such that it is able to
Avoid producing error when gas analysis system is calibrated.
Embodiment four
The structured flowchart of a kind of Standard Gases generation control system that Fig. 4 provides for the another embodiment of the application.
As shown in Figure 4, the present embodiment is to be additionally arranged output module 50 on the basis of a upper embodiment.
Output module 50 is after as operator by the control knob input and output instruction of standard gas distribution meter, by upper
Face obtain for reflecting that the actual volume value of actual volume is exported, the mode of output can be print or utilize display
Equipment shows, thus allows the operator to intuitively obtain this actual volume.
Embodiment five
Present embodiments providing a kind of standard gas distribution meter, this standard gas distribution meter is provided with the mark that above example provides
Quasi-gas generation control system.For the ease of operation, this distributing instrument includes the face being provided with control knob, handle and display device
Plate, is provided with output control knob on panel, for receiving the output order of operator's input.
In this specification, each embodiment uses the mode gone forward one by one to describe, and what each embodiment stressed is and other
The difference of embodiment, between each embodiment, identical similar portion sees mutually.Upper to the disclosed embodiments
State bright, make professional and technical personnel in the field be capable of or use the application.To the multiple amendment of these embodiments to ability
Will be apparent from for the professional and technical personnel in territory, generic principles defined herein can be without departing from the application's
In the case of spirit or scope, realize in other embodiments.Therefore, the application be not intended to be limited to shown in this article these
Embodiment, and it is to fit to the widest scope consistent with principles disclosed herein and features of novelty.
Claims (11)
1. a Standard Gases generation control method under operating mode, is applied to standard gas distribution meter, it is characterised in that include walking as follows
Rapid:
Acquisition is transported to the reagent volume of the reagent in the heating and gasifying mixing bunker of described standard gas distribution meter；
Temperature sensor is utilized to obtain the working temperature under current working；
Utilize the ideal gas formula preset that described working temperature is calculated, obtain revising gasification coefficient；
Described gasification coefficient of revising is utilized described reagent volume to be calculated, after obtaining under current working the gasification of described reagent
The actual volume of reagent gas.
2. Standard Gases generation control method as claimed in claim 1, it is characterised in that described acquisition is transported to described standard
The reagent volume of the reagent in the heating and gasifying mixing bunker of gas distributing instrument, including:
Obtain the reagent volume of the reagent of the peristaltic pump output of described standard gas distribution meter.
3. Standard Gases generation control method as claimed in claim 1, it is characterised in that the preferable gaseous state side that described utilization is preset
Described working temperature is calculated by journey, obtains revising gasification coefficient, including:
It is added described 298.15 with described working temperature, obtains both sums；
By 298.15 divided by described and, obtain corrected parameter；
Default gasification constant is multiplied by described corrected parameter, obtains described correction gasification coefficient.
4. Standard Gases generation control method as claimed in claim 1, it is characterised in that described gasification constant is 1244.
5. the Standard Gases generation control method as described in any one of Claims 1 to 4, it is characterised in that further comprise the steps of:
Output reflects the actual volume value of described actual volume.
6. a Standard Gases generation control system under operating mode, is applied to standard gas distribution meter, it is characterised in that including:
First acquisition module, the examination of the reagent in obtaining the heating and gasifying mixing bunker being transported to described standard gas distribution meter
Agent volume；
Second acquisition module, for receiving the working temperature under the current working that temperature sensor detects；
First computing module, for utilizing default ideal gas formula to calculate described working temperature, obtains revising gas
Change coefficient；
Second computing module, is used for utilizing described gasification coefficient of revising to calculate described reagent volume, obtains current working
Under the actual volume of reagent gas after the gasification of described reagent.
7. Standard Gases generation control system as claimed in claim 6, it is characterised in that described second acquisition module specifically for
Obtain the reagent volume of the reagent of the peristaltic pump output of described standard gas distribution meter.
8. Standard Gases generation control system as claimed in claim 6, it is characterised in that described first computing module includes:
Adder unit, for being added described 298.15 with described working temperature, obtains both sums；
Divider, for by 298.15 divided by described and, obtain corrected parameter；
Multiplication unit, for default gasification constant is multiplied by described corrected parameter, obtains described correction gasification coefficient.
9. Standard Gases generation control system as claimed in claim 6, it is characterised in that described gasification constant is 1244.
10. the Standard Gases generation control system as described in any one of claim 6～9, it is characterised in that also include:
Output module, for exporting the actual volume value reflecting described actual volume.
11. 1 kinds of standard gas distribution meters, it is characterised in that include that the Standard Gases as described in any one of claim 6～10 occurs
Control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610394632.XA CN106093301B (en) | 2016-06-06 | 2016-06-06 | Standard gas generation control method and system under working condition and standard gas distribution instrument |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610394632.XA CN106093301B (en) | 2016-06-06 | 2016-06-06 | Standard gas generation control method and system under working condition and standard gas distribution instrument |
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| Publication Number | Publication Date |
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| CN106093301A true CN106093301A (en) | 2016-11-09 |
| CN106093301B CN106093301B (en) | 2020-09-15 |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6098523A (en) * | 1997-07-10 | 2000-08-08 | Draeger Safety, Inc. | Testing apparatus for gas sensors |
| CN102736645A (en) * | 2012-06-28 | 2012-10-17 | 北京雪迪龙科技股份有限公司 | Standard gas distributing instrument and temperature compensation control device and temperature compensation method |
| CN102749422A (en) * | 2012-07-16 | 2012-10-24 | 北京雪迪龙科技股份有限公司 | Mercury standard gas generating device |
| CN103728421A (en) * | 2014-01-07 | 2014-04-16 | 北京雪迪龙科技股份有限公司 | Element mercury standard gas preparation method and element mercury standard gas preparation system |
-
2016
- 2016-06-06 CN CN201610394632.XA patent/CN106093301B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6098523A (en) * | 1997-07-10 | 2000-08-08 | Draeger Safety, Inc. | Testing apparatus for gas sensors |
| CN102736645A (en) * | 2012-06-28 | 2012-10-17 | 北京雪迪龙科技股份有限公司 | Standard gas distributing instrument and temperature compensation control device and temperature compensation method |
| CN102749422A (en) * | 2012-07-16 | 2012-10-24 | 北京雪迪龙科技股份有限公司 | Mercury standard gas generating device |
| CN103728421A (en) * | 2014-01-07 | 2014-04-16 | 北京雪迪龙科技股份有限公司 | Element mercury standard gas preparation method and element mercury standard gas preparation system |
Non-Patent Citations (1)
| Title |
|---|
| 杨建华: "《大学物理》", 30 April 2016 * |
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| CN106093301B (en) | 2020-09-15 |
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