CN209687687U - A kind of compressor collector - Google Patents
A kind of compressor collector Download PDFInfo
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- CN209687687U CN209687687U CN201822226949.XU CN201822226949U CN209687687U CN 209687687 U CN209687687 U CN 209687687U CN 201822226949 U CN201822226949 U CN 201822226949U CN 209687687 U CN209687687 U CN 209687687U
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Abstract
The utility model belongs to gas compression processing technology field, and in particular to a kind of compressor collector and method.Include: gas main, take tracheae, one end is extend into inside the gas main, and the other end is connected with compressor;It preferably, further include diversion belt, the outside for taking tracheae is arranged in spiral, for changing the conveying direction of impure gas in the gas main.After impure gas encounters diversion belt in gas main road, change airflow direction, helical flow has been changed to by streamlined flow, the solid dust in gas is got off under the action of centrifugal force (or gravity) by the inner wall supplementary set of gas main, and prolong airflow direction, continue to be fed forward.And in the position for taking gas section import, that is, tube hub position, clean gas area is formed, the dust in clean gas area substantially reduces, and separative efficiency is 90% or more.
Description
Technical field
The utility model belongs to gas compression processing technology field, and in particular to a kind of compressor collector.
Background technique
Gas has compressibility, and the gas after compressor does mechanical work to make volume-diminished itself, pressure raising is pressure
Contracting gas.Compressed gas is important power source, is to be only second to the second largest power source of electric power, and serve many purposes
Technique gas source, application range throughout petroleum, chemical industry, metallurgy, electric power, machinery, light industry, weaving, automobile manufacture, electronics, food,
A variety of industries and the departments such as medicine, biochemical, national defence and scientific research.
Conventionally, as the air or the process gas in production itself of nature can contain some particulate matters etc.
Impurity necessarily has partial impurities to be mixed into compressed gas when carrying out compression work, and the compression for causing compressor to generate is empty
Gas be it is unpurified, while the impurity such as dust or particulate matter can on pipeline and the process component of compressor on fouling, cause be
System and equipment are blocked quickly or even whole device parking.
It is existing in order to overcome the problems, such as that compressed gas is brought in production process to product quality and compressor pneumatic circuit etc.
The solution for having technology is mostly that dust-extraction unit is arranged on pipeline, is dusted processing to gas in advance or after compression.Example
Such as, Chinese patent literature CN206715495U discloses a kind of compressed air purifying processing unit, including air compressor, compression
Air storage tank, W type gravity bend pipe and two oil water separators, by being added between compressed air reservoir and air hatch
W type gravity bend pipe, and level-one oil water separator and second level is respectively set in two bottoms of the W type gravity bend pipe on gas circuit direction
Oil water separator makes to be mixed into the impurity such as a small amount of elaioleucite in compressed air since the effect of gravity is slipped to along W type gravity bend pipe
In oil water separator, and by level-one oil water separator and second level oil water separator, reach that completely remove mixed elaioleucite etc. miscellaneous
The purpose of matter.
However, main problem existing for above-mentioned modified compressed air treatment device is: (1) equipment investment increases, land occupation
Area is big;(2) increase system resistance, the power consumption of compressor increases;(3) equipment needs periodic maintenance, as oil water separator is main
Periodic cleaning etc., maintenance cost is higher.
In conclusion how overcoming the defect in the presence of the prior art in the research and development of compressor assembly, providing
A kind of structure is simple, does not increase system resistance, is easy to maintain, and good dedusting effect meets subsequent technique to compressed gas cleanliness
It is required that compressor collector be major issue urgently to be resolved at present.
Utility model content
Therefore, the technical problem to be solved by the present invention is to overcome, in the prior art structure is complicated, occupied area
Greatly, increase system resistance and power consumption, the defects of inconvenient is safeguarded, to provide a kind of compressor collector.
In order to solve the above technical problems, the utility model adopts the following technical solution:
A kind of compressor collector, comprising:
Gas main, the conveying for impure gas;
Tracheae is taken, one end is extend into inside the gas main, and the other end is connected with compressor;
Wherein, the one end extending into inside gas main is to take gas section, takes the opening direction of gas section and the gas main
In impure gas conveying direction it is identical, for obtaining the impure gas in gas main;The other end is air outlet section, is used for
Gas is provided for compressor.
Specifically, one end inlet end of the gas main, the other end are outlet side, do not enter the process gas for taking tracheae
It can be used for washing, cooling or send other devices outside.
Further, the compressor collector further includes diversion belt, and the outside for taking tracheae is arranged in spiral, is used
In the conveying direction for changing impure gas in the gas main.
Further, described to take tracheae further include bend loss, is set to described take between gas section and air outlet section.
Further, the distance between the position for taking gas section to be open and gas main's inlet end are greater than 3 times of gas
The diameter of body general pipeline.
Further, the open end for taking gas section is tilted to the impure gas conveying direction;
Preferably, tilt angle is 15-75 °.
Further, the width of the diversion belt is 0.05-0.4 times of gas main's diameter.
Further, the diameter for taking tracheae is (0.1-0.8) times of gas main's diameter.
Further, the winding circle number of the diversion belt is 1-10 circle, and spacing is (0.5-3) of gas main's diameter
Times.
Further, one end that the air outlet section is connected with compressor reaches the outside of the gas main.
The utility model the application method of compressor collector is also provided the following steps are included:
It is passed through impure gas in the gas main, starts compressor, the impure gas, which flows through, to be taken outside tracheae
Portion takes pipe by taking the opening of gas section to enter, and by air outlet section, provides gas for compressor, completion takes gas.
Further, the flow velocity of impure gas is 8-50 meter per second in the gas main.
Technical solutions of the utility model have the advantages that
1. compressor collector provided by the utility model, comprising: gas main, the conveying for impure gas;
Tracheae is taken, one end is extend into inside the gas main, and the other end is connected with compressor;Wherein, it extend into gas main
The one end in portion is to take gas section, takes the opening direction of gas section identical as the conveying direction of impure gas in the gas main, is used
Impure gas in acquisition gas main;The other end is air outlet section, for providing gas for compressor.The device is suitable for
The relatively little of occasion of dust content, gas velocity of the impure gas in gas main is higher, dust under the effect of gravity with gas
It realizes separation, achieves the desired results, the resistance of system is less than the individual dust-extraction units such as sack cleaner and cyclone separator, pressure
Power loss is smaller.
Compressor collector provided by the utility model preferably further includes diversion belt, and spiral, which is arranged, takes gas described
The outside of pipe, for changing the conveying direction of impure gas in the gas main.Impure gas is in gas main road
After encountering diversion belt, changes airflow direction, helical flow has been changed to by streamlined flow, and control the flow velocity of helical flow in 15-
50m/s, the solid dust in gas is got off by the inner wall supplementary set of gas main under the influence of centrifugal force, and prolongs airflow direction,
Continue to be fed forward.And in the position for taking gas section import, that is, tube hub position, form clean gas area, clean gas area
Interior dust substantially reduces, and separative efficiency is 90% or more.
Compressor collector provided by the utility model, described to take tracheae further include bend loss, is set to described
It takes between gas section and air outlet section.The bend pipe can be realized draws gas main for gas nearby, and plays fixation and take tracheae position
The effect set.
Compressor collector provided by the utility model, it is described take gas section be open position and gas main's inlet end it
Between distance be greater than 3 times of gas mains diameter, it is relatively uniform can to guarantee that gas and solid are distributed in pipeline, then pass through
Diversion belt is crossed, effective cyclonic separation is carried out.The open end for taking gas section inclines with to the impure gas conveying direction
Tiltedly, it is preferred that tilt angle is 15-75 °, and its purpose is to guarantee that gas section opening is taken not have dust accumulation to cause to take gas
Mouth blocking.
Compressor collector provided by the utility model, the width of the diversion belt are gas main's diameter
0.05-0.4 times;The winding circle number of diversion belt is 1-10 circle, and spacing is (0.1-0.8) times of gas main's diameter;It is described to take
The diameter of tracheae is (0.5-3) times of gas main's diameter;The reasonable setting and optimization of the above parameter, can rationally control gas
Body flow velocity not only can guarantee guarantee separating effect, but also not will increase technique resistance, and energy consumption not will increase dramatically.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the first embodiment of the utility model;
Fig. 2 is the structural schematic diagram of second of embodiment of the utility model
Fig. 3 is the structural schematic diagram of the third embodiment of the utility model.
Description of symbols:
1- gas main, 2- take tracheae, 3- air outlet section, and 4- takes gas section, 5- diversion belt, 6- bend loss, wherein arrow
Head represents gas flow direction.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical
Novel protected range.
It is in the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection;It can be mechanical connection, be also possible to be electrically connected;Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
The concrete meaning of language in the present invention.
In addition, as long as technical characteristic involved in the utility model different embodiments disclosed below is each other
Not constituting conflict can be combined with each other.
Embodiment 1
The present embodiment provides a kind of compressor collectors, include as shown in Figure 1, horizontally disposed gas main 1;Take gas
Pipe 2, including gas section 4 and air outlet section 3 are taken, it takes gas section 4 to extend into inside gas main, takes the opening direction and the gas of gas section
The conveying direction of impure gas is identical in general pipeline, and the open end for taking gas section 4 is to the impure gas conveying direction
Inclination, tilt angle are 45 °, the outside also spiral for taking gas section 4 are provided with diversion belt 5, winding circle number is five circles, air outlet section 3
The outside for reaching gas main 1 is connected with compression extraction air mouth by pipeline.
In the present embodiment, the diameter of gas main 1 is 1500 millimeters, and the position for taking gas section 4 to be open is away from gas main's 1
The distance of inlet end is 5000 millimeters, and taking the diameter of tracheae is 500 millimeters, and the width of diversion belt is 100 millimeters, spacing 1000
Millimeter.
Specific application method are as follows: enter impure gas in gas main with the speed of 45 meter per seconds, impure gas
Body flows in gas main, after encountering diversion belt 5, changes gas flow, has been changed to helical flow, spiral flow by streamlined flow
Dynamic flow velocity is 35m/s, and the solid dust in gas is got off by the inner wall supplementary set of gas main 1 under the influence of centrifugal force, and
Prolong airflow direction, continue to be fed forward, in the position for taking gas section to be open, that is, tube hub position, forms clean gas area, it is clean
Dust in net gas zone substantially reduces, and gas is entered under the action of compression extraction air pipe and taken in tracheae 2, and passes through outlet
Section is conveyed to compressor, and completion takes gas;It does not enter and the gas in tracheae 2 is taken to prolong gas main's continuation flow forward, remove cold air
Cold air of the blower as crystallizer.
Embodiment 2
The present embodiment provides a kind of compressor collectors, include as shown in Figure 2, horizontally disposed gas main 1;Take gas
Pipe 2 takes gas section 4, bend loss 6 and air outlet section 3 including what is be sequentially communicated, takes gas section 4 to extend into inside gas main, take gas section
Opening direction is identical as the conveying direction of impure gas in the gas main, and the open end for taking gas section 4 is to described
Impure gas conveying direction inclination, tilt angle is the outside that 45 ° of air outlet sections 3 reach gas main 1, with compression extraction air
Mouth is connected by pipeline.
In the present embodiment, the diameter of gas main 1 is 1000 millimeters, and the position for taking gas section 4 to be open is away from gas main's 1
The distance of inlet end is 4000 millimeters, and taking the diameter of tracheae is 800 millimeters.
Specific application method are as follows: the device is suitable for the less occasion of dust content, by impure gas with 30 meters/
Second speed enter in gas main, impure gas flows in gas main, the solid dust in gas in gravity and
Got off under the action of inertia force by the inner wall supplementary set of gas main 1, and prolong airflow direction, continues to be fed forward, flow to and take gas
The dust content of 4 aperture positions of section substantially reduces, and gas is entered under the action of compression extraction air pipe and taken in tracheae 2, and is led to
It crosses air outlet section and is conveyed to compressor, completion takes gas;It does not enter and the gas in tracheae 2 is taken to prolong gas main's continuation flow forward,
Go scrubbing tower, the process gas after wash cooling.
Embodiment 3
The present embodiment provides a kind of compressor collectors, include as shown in Figure 3, horizontally disposed gas main 1;Take gas
Pipe 2 takes gas section 4, bend loss 6 and air outlet section 3 including be sequentially communicated setting, takes gas section 4 to extend into inside gas main, take gas
Section opening direction it is identical as the conveying direction of impure gas in the gas main, the open end for taking gas section 4 to
The impure gas conveying direction inclination, tilt angle is 45 °, and the outside also spiral for taking gas section 4 is provided with diversion belt 5,
Winding circle number is four circles, and air outlet section 3 reaches the outside of gas main 1, is connected with compression extraction air mouth by pipeline.
In the present embodiment, the diameter of gas main 1 is 800 millimeters, and the position for taking gas section 4 to be open is away from gas main's 1
The distance of inlet end is 2500 millimeters, and taking the diameter of tracheae is 400 millimeters, and the width of diversion belt is 50 millimeters, and spacing is 400 millis
Rice.
Specific application method are as follows: enter impure gas in gas main with the speed of 30 meter per seconds, impure gas
Body flows in gas main, after encountering diversion belt 5, changes gas flow, has been changed to helical flow, spiral flow by streamlined flow
Dynamic flow velocity is 20m/s, and the solid dust in gas is got off by the inner wall supplementary set of gas main 1 under the influence of centrifugal force, and
Prolong airflow direction, continue to be fed forward, in the position for taking gas section to be open, that is, tube hub position, forms clean gas area, it is clean
Dust in net gas zone substantially reduces, and gas is entered under the action of compression extraction air pipe and taken in tracheae 2, and passes through outlet
Section is conveyed to compressor, and completion takes gas;It does not enter and the gas in tracheae 2 is taken to prolong gas main's continuation flow forward, remove tail gas
Processing unit is further processed.
Application example: the application of this technique and device in Melamine Production
In melamine preparation device, the carrier gas of melamine compressor comes from trap, the technique come out in trap
Containing the melamine powder not removed largely, and the melamine gas not being fully crystallized in gas, for this experiment
Solid content is 40mg/L in gas, and average grain diameter is 30 microns, and melamine solid first can be on conveyance conduit, compressor
Wall is tied at the positions such as import, the positions such as incomplete melamine gas also will continue on pipeline, compressor inlet knot wall, existing
Using the methods of scrubbing tower, filter, the dust in gas is removed, it is big that there are system resistance, compressor power consumption height, equipment investment
Greatly, the problems such as equipment cycle of operation section, overhaul of the equipments heavy workload.
Now carry out taking gas using collector provided by the utility model, method particularly includes: it is provided using embodiment 1-3
Collector, gas be responsible in gas velocity take 30m/s, diversion belt spiral is set as 4 circles, and gas main is straight tube, dusty gas
After encountering hurricane band in pipeline, changes airflow direction, helical flow has been changed to by streamlined flow, the flow velocity of helical flow is
20m/s, the solid dust in gas is got off by the inner wall supplementary set of gas main under the influence of centrifugal force, and prolongs airflow direction,
Continue to be fed forward.And in the position for taking gas section to be open, that is, tube hub position, form clean gas area, clean gas area
Interior dust substantially reduces, the separative efficiency of the dust of different-grain diameter referring to embodiment 3 in following table data.By cyclonic separation
Clean gas afterwards passes sequentially through and takes gas inlet pipe, bend pipe and take gas outlet, drawn outside process gas general pipeline processed, then
The import of compressor need to can be only directly connected to by pipeline.
Referring to the specific embodiment that Fig. 1, embodiment 1 are provided, it can also be not provided with bend pipe, concrete outcome see the table below embodiment
1 data.
Relatively smaller containing Dust Capacity for gas, the biggish occasion of particle can cancel diversion belt, as shown in Figure 2.Because of gas
The gas velocity of general pipeline is very high, and in 30 meter per second, a small amount of dust equally plays certain separation and make under the action of inertia force
With, effect referring to the data of following table embodiment 2.
1 separating effect of table
Granular size | The prior art | Embodiment 1 | Embodiment 2 | Embodiment 3 |
100(μm) | 100% | 0% | 0% | 0% |
50(μm) | 100% | 0% | 0% | 0% |
30(μm) | 100% | 0% | 0% | 0% |
20(μm) | 100% | 0% | 3% | 0% |
10(μm) | 100% | 15% | 22% | 10% |
5(μm) | 100% | 30% | 41% | 14% |
1(μm) | 100% | 40.8% | 51.6% | 28% |
Obviously, the above embodiments are merely examples for clarifying the description, and does not limit the embodiments.It is right
For those of ordinary skill in the art, can also make on the basis of the above description it is other it is various forms of variation or
It changes.There is no necessity and possibility to exhaust all the enbodiments.And it is extended from this it is obvious variation or
It changes among the protection scope created still in the utility model.
Claims (10)
1. a kind of compressor collector characterized by comprising
Gas main, the conveying for impure gas;
Tracheae is taken, one end is extend into inside the gas main, and the other end is connected with compressor;
Wherein, the one end extending into inside gas main is to take gas section, takes in the opening direction of gas section and the gas main and contains
Foreign gas it is identical, for obtaining the impure gas in gas main;The other end is air outlet section, for providing for compressor
Gas.
2. compressor collector according to claim 1, which is characterized in that further include diversion belt, spiral is arranged in institute
The outside for taking tracheae is stated, for changing the conveying direction of impure gas in the gas main.
3. compressor collector according to claim 1 or 2, which is characterized in that it is described that take tracheae further include bend loss,
It is set to described take between gas section and air outlet section.
4. compressor collector according to claim 1 or 2, which is characterized in that it is described take gas section be open position with
The distance between gas main's inlet end is greater than the diameter of 3 times of gas mains.
5. compressor collector according to claim 1 or 2, which is characterized in that the open end for taking gas section to
The impure gas conveying direction inclination.
6. compressor collector according to claim 5, which is characterized in that the open end for taking gas section is to described
The impure inclined angle of gas conveying direction is 15-75 °.
7. compressor collector according to claim 2, which is characterized in that the width of the diversion belt is the gas
0.05-0.4 times of total pipe diameter.
8. compressor collector according to claim 1 or 2, which is characterized in that the diameter for taking tracheae is gas
0.1-0.8 times of total pipe diameter.
9. compressor collector according to claim 2, which is characterized in that the winding circle number of the diversion belt is 1-
10 circles, spacing are 0.5-3 times of gas main's diameter.
10. compressor collector according to claim 1 or 2, which is characterized in that the air outlet section is connected with compressor
Logical one end reaches the outside of the gas main.
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CN201822226949.XU CN209687687U (en) | 2018-12-27 | 2018-12-27 | A kind of compressor collector |
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CN201822226949.XU CN209687687U (en) | 2018-12-27 | 2018-12-27 | A kind of compressor collector |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109578251A (en) * | 2018-12-27 | 2019-04-05 | 四川金象赛瑞化工股份有限公司 | A kind of compressor collector and method |
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2018
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109578251A (en) * | 2018-12-27 | 2019-04-05 | 四川金象赛瑞化工股份有限公司 | A kind of compressor collector and method |
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