CN204620442U - A kind of standard particle generating means - Google Patents
A kind of standard particle generating means Download PDFInfo
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- CN204620442U CN204620442U CN201520259725.2U CN201520259725U CN204620442U CN 204620442 U CN204620442 U CN 204620442U CN 201520259725 U CN201520259725 U CN 201520259725U CN 204620442 U CN204620442 U CN 204620442U
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- negative pressure
- generating means
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- knockout drum
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Abstract
The utility model relates to dust concentration and Powder Particle Size demarcates field, has particularly related to a kind of standard particle generating means.This standard particle generating means comprises valve actuating mechanism and the boiling type particle sieve series device arranged one on the other and bucket type particle sorting apparatus, described boiling type particle sieve series device comprises housing, be located at least one deck screen cloth in housing and be connected with housing, inflatable body for making the particle on screen cloth form fluid boiling state; Bucket type particle sorting apparatus comprises knockout drum, is connected with negative pressure and inhales sub-agencies between the upper and lower end of knockout drum; Inflatable body and negative pressure are inhaled sub-agencies and are all connected with valve actuating mechanism, and the housing of boiling type particle sieve series device is connected with knockout drum by the outlet set by bottom.The utility model solves low, the ropy problem of existing standard particle make efficiency.
Description
Technical field
The utility model relates to dust concentration and Powder Particle Size demarcates field, has particularly related to a kind of standard particle generating means.
Background technology
Sensor of dust concentration needs dust test wind tunnel simulation dust atmosphere when demarcating and examine and determine elementary error, so just needs dust generator to send dust in wind-tunnel.According to the regulation of MT/T1102-2009 mining dust concentration sensor, in dust test wind-tunnel, the particle diameter of coal dust should be less than 74 μm, and the particle being wherein less than 10 μm accounts for 10% ~ 15%, and the particle being less than 30 μm accounts for 47 % ~ 50 %.Generally that employing standard sieve obtains the particle of test by the method for repeatedly sieving in prior art.
When the online particles distribution instrument of Coal Transportation System is examined and determine, need a particle size distribution environment determined to examine and determine, the general purchase standard particle that adopts is examined and determine.
Prior art can meet the needs of instrumental calibration to a certain extent, but but there is following problem: 1, sieve screening time-consuming, effort and harm can be produced to personnel health, in addition, sieve can only control the upper limit of particle diameter,, there is comparatively big error in the lower limit of uncontrollable particle and size distribution; 2, the particle size range of sieve screening controls inaccurate, cannot meet the requirement of the standard particle that particle size analyzer is demarcated; 3, the cost of standard particle is higher, and standard particle mostly is the physics of synthetic plastic and coal dust and chemical property there are differences, and affects measurement result accuracy; 4, for the sensor of dust concentration matched curve of MIEShi scattering theory, because average particle size determines experiment curv slope, the control that cannot realize average grain diameter is sieved, so the accurate measurement that can not be used for granule density or granularity is sent out in screening.
In sum, the standard particle that current employing screening mode obtains also exists the problem that make efficiency is low, granular mass is poor.It is higher to there is cost in the standard particle thing simultaneously bought, and there is different in kind, cause measure error with coal dust.
Utility model content
The purpose of this utility model is to provide a kind of standard particle generating means, to solve low, the ropy problem of existing standard particle make efficiency.
In order to solve the problem, standard particle generating means of the present utility model is by the following technical solutions: standard particle generating means, comprise valve actuating mechanism and the boiling type particle sieve series device arranged one on the other and bucket type particle sorting apparatus, described boiling type particle sieve series device comprise housing, be located at least one deck screen cloth in housing and be connected with housing, inflatable body for making the particle on screen cloth form fluid boiling state; Bucket type particle sorting apparatus comprises knockout drum, is connected with negative pressure and inhales sub-agencies between the upper and lower end of knockout drum; Inflatable body and negative pressure are inhaled sub-agencies and are all connected with valve actuating mechanism, and the housing of boiling type particle sieve series device is connected with knockout drum by the outlet set by bottom.
Described inflatable body comprises the blowing sprayer corresponding with screen cloth, described blowing sprayer be located at the below place of corresponding screen cloth and blowing direction towards corresponding screen cloth.
The inlet end place of described blowing sprayer is provided with negative pressure generator tube, described negative pressure generator tube be inserted in blowing sprayer inlet end and with blowing sprayer matched in clearance, blowing sprayer is connected with valve actuating mechanism by described negative pressure generator tube.
Described negative pressure is inhaled sub-agencies and is comprised suction pipe, and suction pipe is connected with knockout drum.
The exit that boiling type particle sieve series device comprises housing is provided with tremie pipe, and housing is connected with knockout drum by described tremie pipe.
Valve actuating mechanism comprises air pump, air pump is inhaled sub-agencies by corresponding pipeline with described inflatable body and negative pressure and is connected, wherein inflatable body and the pipeline between negative pressure suction sub-agencies and air pump are respectively equipped with pneumatic air extractor, described pneumatic air extractor comprises tracheae, one end of tracheae is provided with inlet scoop, the other end is provided with exhaust outlet, in addition, ring-like gas chamber is provided with in the wall of tracheae, ring-like gas chamber has import and which is provided with the air cleft be communicated with tracheae endoporus, air pump is connected with the import of ring-like gas chamber, inflatable body is connected with the exhaust outlet of pneumatic air extractor, negative pressure is inhaled sub-agencies and is connected with the inlet scoop of pneumatic air extractor.
Described negative pressure is inhaled between sub-agencies and corresponding pneumatic air extractor and is provided with air volume regulating valve.
Described negative pressure is inhaled between sub-agencies and corresponding pneumatic air extractor and is provided with air gauge.
Also be provided with described pneumatic air extractor between air pump and the outlet of knockout drum, the outlet of knockout drum is connected with the negative-pressure air-suction mouth of pneumatic air extractor.
When using this standard particle generating means production standard particle, particle can be placed in boiling type particle sieve series device, under the effect of inflatable body, be arranged in particle on screen cloth less fall to carrying out next stage screening through screen cloth, the particle that larger particle then mutually collides or collides with sieve series device and formed by screen cloth in the process of boiling, particle through sieve series device is falling into knockout drum, because knockout drum internal volume is relatively large, gas flow rate with particle reduces, and the particle in certain particle size range will accelerate under gravity, remaining particle then suspends in atmosphere, now inhale the effect of sub-agencies in negative pressure under, utilize constant speed principle of bleeding the particle of suspension can be siphoned away, due to the acting in conjunction of particle gravity and air-flow, the particle siphoned away and the grain diameter of sedimentation can control within the specific limits, be exactly the accurate control realizing grain diameter like this, abandoned the method for Traditional Man screening simultaneously, the make efficiency of standard particle have also been obtained great raising.In sum, the utility model solves low, the ropy problem of existing standard particle make efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of standard particle generating means;
Fig. 2 is the structural representation of boiling type particle sieve series device;
Fig. 3 is the structural representation of pneumatic air extractor.
Detailed description of the invention
The embodiment of standard particle generating means, as Figure 1-3, this standard particle generating means comprises valve actuating mechanism, boiling type particle sieve series device and bucket type particle sorting apparatus, wherein boiling type particle sieve series device and bucket type particle sorting apparatus are arranged one on the other, and the two forms one-level, the secondary sorting unit of standard particle respectively successively.
The pipeline that valve actuating mechanism comprises air pump 11 and is connected with air pump 11, in the present embodiment, pipeline is specifically divided into three tunnels in parallel mutually, three tunnels are respectively equipped with pneumatic air extractor 12, pneumatic air extractor 12 comprises tracheae, one end of tracheae is provided with inlet scoop 101, the other end is provided with exhaust outlet 102, in addition, ring-like gas chamber 103 is provided with in the wall of tracheae, ring-like gas chamber 103 has import and which is provided with the air cleft be communicated with tracheae endoporus, the gas sprayed by air cleft from ring-like gas chamber during use is blown away along the inwall of tracheae to tracheae exhaust outlet 102, simultaneously, the inlet scoop 101 of tracheae forms negative pressure, and then by the air accelerated band in the external world to exhaust outlet.In the present embodiment, tracheae is formed by an interior pipe 121 and the grafting of an outer tube 122, ring-like gas chamber 103 is surrounded together by interior tube and tube, air cleft between interior pipe and the respective end of outer tube, tracheae respectively with the inlet communication of the ring-like gas chamber of corresponding pneumatic air extractor.
Boiling type particle sieve series device comprises housing 13, be located at the screen cloth in housing 13 and be connected with housing 13, inflatable body for making the particle on screen cloth form fluid boiling state, in the present embodiment, housing 13 is in tubular, screen cloth is provided with two-layer, wherein the mesh of upper strata screen cloth 14 is greater than the mesh of lower screen 15, inflatable body comprises blowing sprayer 16, blowing sprayer 16 is corresponding to screen cloth and be positioned at the below place of corresponding screen cloth, in the present embodiment, two blowing sprayers corresponding with two screen clothes cross mutually and share an air inlet, in addition, the inlet end place of blowing sprayer 16 is provided with negative pressure generator tube 17, negative pressure generator tube 17 be inserted in blowing sprayer inlet end and with blowing sprayer matched in clearance, blowing sprayer 16 is connected with a wherein branch road of valve actuating mechanism by negative pressure generator tube 17, pneumatic air extractor on this branch road is connected with negative pressure generator tube 17 by exhaust outlet, in such cases, when booster air pump 11, then blowing sprayer 16 will make it to form the fluidized state (fluidization) being similar to boiling by the particle upwards brushed on corresponding screen cloth, thus the particle making particle diameter less is fallen by screen cloth, the particle that particle diameter is larger collides with each other and to collide with housing and fragmentation diminishes, until fallen by screen cloth, in the process, due to the existence of negative pressure generator tube 17, Dual-Phrase Distribution of Gas olid is induced to move downward in the gap that in housing, the particle at some dead angle places will be inhaled between negative pressure generator tube 17 and blowing sprayer 16.
Bucket type particle sorting apparatus comprises knockout drum 18, be connected with negative pressure between the upper and lower end of knockout drum 18 and inhale sub-agencies, the housing 13 of boiling type particle sieve series device is connected with knockout drum by the outlet set by bottom, in the present embodiment, the exit of the housing 13 of boiling type particle sieve series device is provided with tremie pipe 19, housing 13 is connected with knockout drum 18 by described tremie pipe 19, and in the present embodiment, tremie pipe 19 is flared tremie pipe.Negative pressure is inhaled sub-agencies and is comprised suction pipe 20, suction pipe 20 is tightly connected in the position at knockout drum about 18 two ends and knockout drum 18, the inlet scoop away from the pneumatic air extractor on one end of knockout drum 18 and a branch road of valve actuating mechanism of suction pipe 20 is connected, in addition, also be provided with air gauge 21 and air volume regulating valve 22 between suction pipe 20 and corresponding pneumatic air extractor, wherein air gauge is differential pressure indicator.
The last item branch road of valve actuating mechanism is connected with the outlet of knockout drum 18, and wherein the outlet of knockout drum 18 is connected with the inlet scoop of the pneumatic air extractor on this branch road.
In use, first booster air pump, air-flow enters each pneumatic air extractor, because the airscoop drag of pneumatic air extractor is larger, air-flow builds pressure in ring-like gas chamber, then from seam discharge, discharged at a high speed by the wall attachment effect of the air-flow exhaust outlet by pneumatic air extractor, inlet scoop place forms negative pressure and air or particle is discharged, as long as so the admission pressure controlling air inlet can control the concentration being vented wind speed and sucking particle.The pneumatic air extractor be connected with boiling type particle sieve series device sprays high velocity air in boiling type particle sieve series device, by negative pressure generator tube to blowing sprayer jet-stream wind, air-flow passes through two screen clothes respectively by blowing sprayer, make particle with air motion, particle forms particle diameter through two screen cloth actings in conjunction and is less than the Dual-Phrase Distribution of Gas olid of setting value and is entered in knockout drum by tremie pipe.Owing to there being slit obliquely between negative pressure generator tube and blowing sprayer, the particle in a part of boiling type particle sieve series device dead angle is taken away in slit place formation negative pressure through out-of-date by air-flow, and induces Dual-Phrase Distribution of Gas olid to move downward.Increase due to knockout drum inner volume makes air-flow velocity reduce, accelerate at Action of Gravity Field bulky grain, the pneumatic air extractor be connected with suction pipe provides suction to suction pipe, the flow velocity sucking air-flow is controlled by air volume regulating valve, illustrate that pumping airflow speed is identical with the air velocity in knockout drum when air gauge (differential pressure indicator) is shown as zero, realize constant speed and bleed, can ensure that the particle suspended is sucked away like this, sedimented particle sedimentation, realizes the accurate control of grain diameter.When using granule, the pneumatic air extractor exhaust outlet be connected with suction pipe is directly connected with wind-tunnel or caliberating device; Opened by the pneumatic air extractor of knockout drum lower end when using bulky grain and be connected with wind-tunnel or caliberating device, the pneumatic air extractor air-flow connected by suction pipe is closed, and exhaust outlet is connected dedusting with dust arrester.Because pneumatic air extractor bore is comparatively large, air-flow velocity is higher, can anti-clogging during for inhaling particle, inspiratory capacity is controlled, and namely particle concentration is controlled.
Claims (9)
1. standard particle generating means, it is characterized in that, comprise valve actuating mechanism and the boiling type particle sieve series device arranged one on the other and bucket type particle sorting apparatus, described boiling type particle sieve series device comprise housing, be located at least one deck screen cloth in housing and be connected with housing, inflatable body for making the particle on screen cloth form fluid boiling state; Bucket type particle sorting apparatus comprises knockout drum, is connected with negative pressure and inhales sub-agencies between the upper and lower end of knockout drum; Inflatable body and negative pressure are inhaled sub-agencies and are all connected with valve actuating mechanism, and the housing of boiling type particle sieve series device is connected with knockout drum by the outlet set by bottom.
2. standard particle generating means according to claim 1, is characterized in that, described inflatable body comprises the blowing sprayer corresponding with screen cloth, described blowing sprayer be located at the below place of corresponding screen cloth and blowing direction towards corresponding screen cloth.
3. standard particle generating means according to claim 2, it is characterized in that, the inlet end place of described blowing sprayer is provided with negative pressure generator tube, described negative pressure generator tube be inserted in blowing sprayer inlet end and with blowing sprayer matched in clearance, blowing sprayer is connected with valve actuating mechanism by described negative pressure generator tube.
4. standard particle generating means according to claim 1, is characterized in that, described negative pressure is inhaled sub-agencies and comprised suction pipe, and suction pipe is connected with knockout drum.
5. standard particle generating means according to claim 1, is characterized in that, the exit that boiling type particle sieve series device comprises housing is provided with tremie pipe, and housing is connected with knockout drum by described tremie pipe.
6. the standard particle generating means according to any one of claim 1-5, it is characterized in that, valve actuating mechanism comprises air pump, air pump is inhaled sub-agencies by corresponding pipeline with described inflatable body and negative pressure and is connected, wherein inflatable body and the pipeline between negative pressure suction sub-agencies and air pump are respectively equipped with pneumatic air extractor, described pneumatic air extractor comprises tracheae, one end of tracheae is provided with inlet scoop, the other end is provided with exhaust outlet, in addition, ring-like gas chamber is provided with in the wall of tracheae, ring-like gas chamber has import and which is provided with the air cleft be communicated with tracheae endoporus, air pump is connected with the import of ring-like gas chamber, inflatable body is connected with the exhaust outlet of pneumatic air extractor, negative pressure is inhaled sub-agencies and is connected with the inlet scoop of pneumatic air extractor.
7. standard particle generating means according to claim 6, is characterized in that, described negative pressure is inhaled between sub-agencies and corresponding pneumatic air extractor and is provided with air volume regulating valve.
8. standard particle generating means according to claim 6, is characterized in that, described negative pressure is inhaled between sub-agencies and corresponding pneumatic air extractor and is provided with air gauge.
9. standard particle generating means according to claim 6, is characterized in that, is also provided with described pneumatic air extractor between air pump and the outlet of knockout drum, and the outlet of knockout drum is connected with the negative-pressure air-suction mouth of pneumatic air extractor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520259725.2U CN204620442U (en) | 2015-04-28 | 2015-04-28 | A kind of standard particle generating means |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520259725.2U CN204620442U (en) | 2015-04-28 | 2015-04-28 | A kind of standard particle generating means |
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| Publication Number | Publication Date |
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| CN204620442U true CN204620442U (en) | 2015-09-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520259725.2U Withdrawn - After Issue CN204620442U (en) | 2015-04-28 | 2015-04-28 | A kind of standard particle generating means |
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| CN (1) | CN204620442U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104801491A (en) * | 2015-04-28 | 2015-07-29 | 郑州光力科技股份有限公司 | Standard particle generating device |
-
2015
- 2015-04-28 CN CN201520259725.2U patent/CN204620442U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104801491A (en) * | 2015-04-28 | 2015-07-29 | 郑州光力科技股份有限公司 | Standard particle generating device |
| CN104801491B (en) * | 2015-04-28 | 2017-04-26 | 郑州光力科技股份有限公司 | Standard particle generating device |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150909 Effective date of abandoning: 20170426 |