CN107352274A - A kind of regulatable new induction Pneumatic conveyer of particle concentration - Google Patents

A kind of regulatable new induction Pneumatic conveyer of particle concentration Download PDF

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Publication number
CN107352274A
CN107352274A CN201710738478.8A CN201710738478A CN107352274A CN 107352274 A CN107352274 A CN 107352274A CN 201710738478 A CN201710738478 A CN 201710738478A CN 107352274 A CN107352274 A CN 107352274A
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CN
China
Prior art keywords
plate
conveying pipeline
air outlet
pneumatic conveying
pneumatic
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Pending
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CN201710738478.8A
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Chinese (zh)
Inventor
刘泽勤
张艺
才爽
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Tianjin University of Commerce
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Tianjin University of Commerce
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Filing date
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Application filed by Tianjin University of Commerce filed Critical Tianjin University of Commerce
Priority to CN201710738478.8A priority Critical patent/CN107352274A/en
Publication of CN107352274A publication Critical patent/CN107352274A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/58Devices for accelerating or decelerating flow of the materials; Use of pressure generators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/52Adaptations of pipes or tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G2201/00Indexing codes relating to handling devices, e.g. conveyors, characterised by the type of product or load being conveyed or handled
    • B65G2201/04Bulk
    • B65G2201/042Granular material

Abstract

The invention discloses a kind of regulatable new induction Pneumatic conveyer of particle concentration, including hollow Pneumatic conveying pipeline, the left and right ends of the Pneumatic conveying pipeline to be separately installed with reducing pipe and increaser;The left and right ends of the reducing pipe have the first air inlet and the first air outlet respectively;The left and right ends of the increaser have the dividing plate and the second air outlet of central aperture respectively;One swivel plate is installed in first air outlet;The inside top wall and bottom inside wall of the Pneumatic conveying pipeline respectively on a particulate generating means is installed;The madial wall of Pneumatic conveying pipeline on the first air outlet opposite position with being provided with interseptal board;Positive the right of interseptal board is provided with a homogenating plate;Vertical plate is also equipped with the madial wall of Pneumatic conveying pipeline;The bottom of vertical plate is provided with blower fan.The present invention during using gas transport particulate matter, can adjust the number concentration of particulate matter in gas according to user's needs, improve the utilization rate of particulate matter.

Description

A kind of regulatable new induction Pneumatic conveyer of particle concentration
Technical field
The present invention relates to strength transmission technique field, more particularly to a kind of regulatable new induction gas of particle concentration Power conveying device.
Background technology
At present, with the startup of China's West-East National Gas Transmission Project, the dredging in rivers navigation channel, the implementation with environmental protection policy is saved, Pipeline is just being widely used in electric power, changed as the fifth-largest means of transportation in addition to railway, highway, water transport, aviation The industries such as work, building materials, metallurgy.One of the major way of Geldart-D particle as pipeline, have other mode of movements not comparable The advantages of plan.The industrial departments such as many pharmacy now, food, plastics, cement, chemical industry, building materials, mining, are generally used Pneumatic Conveying Technology conveys different particles, and its principle is by the use of air-flow (air or inert gas) as carrier, in pipeline In conveying powdered and granular solid particulate matter.
For Pneumatic conveyer, reduce air velocity, improve number concentration (the i.e. unit bodies pneumatosis of particulate matter in gas The particulate matter number contained in body, and the number concentration of the particulate matter in Pneumatic conveying pipeline) it is to improve its transfer efficiency It is crucial.But not all industrial department is required for the number concentration of very high particulate matter, also has industrial department to need basis Production is needed to regulate and control the number concentration of particulate matter in gas, and so as to improve the utilization rate of particulate matter, still, there is presently no one Kind Pneumatic conveyer, it can adjust gas according to the needs of user in real time during using gas transport particulate matter The number concentration of particulate matter in body, meet varying number concentration necessary of the user to particulate matter in gas of different purposes.
Therefore, at present there is an urgent need to develop a kind of technology, it can be real during using gas transport particulate matter When according to the needs of user adjust the number concentration of particulate matter in gas, meet the user of different purposes to particulate matter in gas Varying number concentration necessary, and then improve particulate matter utilization rate.
The content of the invention
In view of this, it is an object of the invention to provide a kind of regulatable new induction Geldart-D particle dress of particle concentration Put, it can adjust particulate matter in gas according to the needs of user in real time during using gas transport particulate matter Number concentration, meet varying number concentration necessary of the user to particulate matter in gas of different purposes, and then improve particulate matter Utilization rate, be advantageous to extensive popularization and application, be of great practical significance.
Therefore, the present invention provides a kind of regulatable new induction Pneumatic conveyer of particle concentration, including it is hollow Pneumatic conveying pipeline, the left and right ends of the Pneumatic conveying pipeline are separately installed with reducing pipe and increaser;
The left and right ends of the reducing pipe have the first air inlet and the first air outlet respectively;
The left and right ends of the increaser have the dividing plate and the second air outlet of central aperture respectively;
One swivel plate is installed in first air outlet;
The inside top wall and bottom inside wall of the Pneumatic conveying pipeline above the reducing pipe are upper respectively to pacify Equipped with a particulate generating means;
The madial wall of the Pneumatic conveying pipeline be provided with the position corresponding with first air outlet one every Between plate;
Positive the right of the interseptal board is provided with a homogenating plate;
A vertical plate is also equipped with the madial wall of the Pneumatic conveying pipeline;
The bottom of the vertical plate is provided with a blower fan.
Wherein, the top and bottom of first air inlet respectively with the inside top wall of the Pneumatic conveying pipeline and bottom The tangent connection of portion's madial wall;
The top and bottom of second air outlet respectively with the inside top wall of the Pneumatic conveying pipeline and bottom The tangent connection of side wall;
The swivel plate is arranged on the vertical direction centre position of first air outlet.
Wherein, position of the particulate generating means between the interseptal board and the first air inlet.
Wherein, the upper and lower ends of the vertical plate inside top wall and bottom inside with the Pneumatic conveying pipeline respectively Wall connects;
The vertical plate is located at the right of the homogenating plate, and the vertical plate is located at the positive left side of the dividing plate.
Wherein, the upper right of the vertical plate is provided with the slideway of a vertical direction distribution, is installed on the slideway There is a sliding panel.
Wherein, the bore of the first air inlet high order end is identical with the caliber of the Pneumatic conveying pipeline;
The bore of first air inlet of the reducing pipe left end from left to right progressively reduces, and the second of the increaser right-hand member The bore of air outlet from left to right incrementally increases.
Wherein, the first raised, compartment opening and the second projection is distributed with the interseptal board in vertical direction;
The front and rear sides inwall of the compartment opening and the angle of vertical plane are equal to 120 degree;
The angle of described first raised front side wall and the second raised rear wall and vertical plane is respectively equal to 120 Degree.
Wherein, the homogenating plate is shaped as V-arrangement, and the left end center of the homogenating plate has tip, the equal wind Both sides have a plate tail to the right-hand member of plate respectively up and down, and the vertical direction centre position of the tip and the interseptal board is located at together In one level height;
Horizontal range between the tip and the plate tail is the mouth of the first air outlet less than the reducing pipe right-hand member The half in footpath.Wherein, the left side edge position of the sliding panel is provided with rubber bar;
The air entry of the blower fan is in the left side of the vertical plate, and the gas outlet of the blower fan is on the right side of the vertical plate Side.
Wherein, longitudinal cross-section of the longitudinal cross-section product of the left end entrance of the increaser more than the vertical plate central opening Product, the caliber of the second air outlet low order end should be identical with the caliber of the Pneumatic conveying pipeline.
The technical scheme provided by the invention more than, compared with prior art, the invention provides a kind of particle The regulatable new induction Pneumatic conveyer of thing concentration, it can be during using gas transport particulate matter, real-time root The number concentration of particulate matter in gas is adjusted according to the needs of user, meets the users of different purposes to particulate matter in gas not With number concentration demand, and then the utilization rate of particulate matter is improved, be advantageous to extensive popularization and application, there are great production practices Meaning.
Brief description of the drawings
Fig. 1 is each possessed by a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention The installation site structure schematic diagram of individual part;
Fig. 2 is reducing pipe in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Fig. 3 is reducing pipe in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Fig. 4 is reducing pipe in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
Fig. 5 is swivel plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Fig. 6 is swivel plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Fig. 7 is swivel plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
Fig. 8 is a kind of regulatable new induction Pneumatic conveyer intermediate chamber plate of particle concentration provided by the invention Front view;
Fig. 9 is a kind of regulatable new induction Pneumatic conveyer intermediate chamber plate of particle concentration provided by the invention Left view;
Figure 10 is a kind of regulatable new induction Pneumatic conveyer intermediate chamber plate of particle concentration provided by the invention Top view;
Figure 11 is homogenating plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Figure 12 is homogenating plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Figure 13 is homogenating plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
Figure 14 is vertical plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Figure 15 is vertical plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Figure 16 is vertical plate in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
Figure 17 is sliding panel in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Figure 18 is sliding panel in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Figure 19 is sliding panel in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
Figure 20 is increaser in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Front view;
Figure 21 is increaser in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Left view;
Figure 22 is increaser in a kind of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention Top view;
In figure, 1 is Pneumatic conveying pipeline, and 2 be reducing pipe, and 3 be particulate generating means, and 4 be swivel plate, and 5 be interseptal board;
51 be first raised, and 52 be compartment opening, and 53 be second raised;
6 be homogenating plate, and 61 be tip, and 62 be plate tail, and 7 be slideway, and 8 be sliding panel, and 80 be rubber bar, and 9 be vertical plate, 10 It is increaser for blower fan, 11;
21 be the first air inlet, and 22 be the first air outlet, and 111 be dividing plate, and 112 be the second air outlet.
Embodiment
In order that those skilled in the art more fully understand the present invention program, below in conjunction with the accompanying drawings with embodiment to this Invention is described in further detail.
Referring to Fig. 1 to Figure 22, the invention provides a kind of regulatable new induction Pneumatic conveyer of particle concentration, It can adjust the quantity of particulate matter in gas according to the needs of user in real time during using gas transport particulate matter Concentration, meet varying number concentration necessary of the user to particulate matter in gas of different purposes.The particle concentration is regulatable New induction Pneumatic conveyer includes hollow Pneumatic conveying pipeline (i.e. airduct) 1, the left and right two of the Pneumatic conveying pipeline 1 End is separately installed with reducing pipe 2 and increaser 11;
The left and right ends of the reducing pipe 2 have the first air inlet 21 and the first air outlet 22, first air intake respectively The top and bottom of mouth 21 are connected with the inside top wall and bottom inside wall of the Pneumatic conveying pipeline 1 respectively (is preferably Tangent connection);
The left and right ends of the increaser 11 have the air outlet 112 of dividing plate 111 and second of central aperture respectively;
The top and bottom of second air outlet 112 the inside top wall with the Pneumatic conveying pipeline 1 and bottom respectively Portion's madial wall is connected (being preferably tangent connection);
One swivel plate 4 is installed, the swivel plate 4 is preferably mounted to described first and gone out in first air outlet 22 The vertical direction centre position in air port 22;
The inside top wall and bottom inside wall of the Pneumatic conveying pipeline 1 above the reducing pipe 2 respectively on One particulate generating means 3 is installed;
The madial wall of the Pneumatic conveying pipeline 1 is provided with one on the position corresponding with first air outlet 22 Interseptal board 5;
Position of the particulate generating means 3 between the air inlet 21 of interseptal board 5 and first;
Positive the right of the interseptal board 5 is provided with a homogenating plate 6;
A vertical plate 9, the upper and lower ends of the vertical plate 9 are also equipped with the madial wall of the Pneumatic conveying pipeline 1 Connect respectively with the inside top wall and bottom inside wall of the Pneumatic conveying pipeline 1;
The vertical plate 9 is located at the right of the homogenating plate 6, and the vertical plate 9 is located at the positive left side of the dividing plate 111;
The upper right of the vertical plate 9 is provided with the slideway 7 of a vertical direction distribution, is provided with the slideway 7 One sliding panel 8, therefore, the sliding panel 8 can vertically be slided in the upper right of the vertical plate 9;
The bottom of the vertical plate 9 is provided with a blower fan 10.
In the present invention, in specific implementation, the Pneumatic conveying pipeline 1 is preferably that longitudinal section is square airduct.
In the present invention, in specific implementation, bore and the Pneumatic conveying pipeline 1 of the high order end of the first air inlet 21 Caliber it is identical.
It should be noted that in the present invention, the bore of the first air inlet 21 of the left end of reducing pipe 2 from left to right by Step reduces, and the bore of the second air outlet 112 of the right-hand member of increaser 11 from left to right incrementally increases.
In the present invention, in specific implementation, the both sides wall surface area of the swivel plate 4 respectively with second air outlet 22 transverse opening longitudinal cross-section product is identical.
In the present invention, in specific implementation, the first projection 51 is distributed with the interseptal board 5 in vertical direction, compartment is opened The projection 53 of mouth 52 and second;
The front and rear sides inwall of the compartment opening 52 and the angle of vertical plane are equal to 120 degree;
The angle of the rear wall and vertical plane of the front side wall of first projection 51 and second projection 53 is respectively equal to 120 degree.
In specific implementation, as the compartment opening 52 of central opening, its longitudinal cross-section product that is open is more than first air-out The opening longitudinal cross-section product of mouth 22.
In the present invention, in specific implementation, the vertical direction centre position of the homogenating plate 6 is hung down with the interseptal board 5 Nogata is located in same level height to centre position;
In specific implementation, the homogenating plate 6 is preferably shaped to V-arrangement, and the left end center of the homogenating plate 6 has point First 61, both sides have a plate tail 62 to the right-hand member of the homogenating plate 6 respectively up and down, and the tip 61 hangs down with the interseptal board 5 Nogata is located in same level height to centre position.
In specific implementation, the horizontal range between the tip 61 and the plate tail 62 is preferably less than the reducing pipe 2 The half of the bore (i.e. caliber) of first air outlet 22 of right-hand member, the horizontal range are the top view of homogenating plate 6 of V-type Width in (Figure 13).In the present invention, in specific implementation, the left side edge position of the sliding panel 8 is provided with rubber Bar 80, by rubber bar 80 gas on the right side of vertical plate 9 can be prevented to suck left side, meanwhile, by the rubber bar 80, can make The sliding panel 8 is obtained when the upper right of the vertical plate 9 is vertically slided, the sliding panel 8 is protected, Avoid sliding panel 8 from being worn and reduce the whole service life of the present invention.
In the present invention, in specific implementation, the central opening longitudinal cross-section product of the vertical plate 9 should be greater than reducing pipe 2 The longitudinal cross-section product of first air outlet, and accumulated less than the opening longitudinal cross-section of interseptal board 5.
In the present invention, in specific implementation, the longitudinal cross-section product of the sliding panel 8 should be greater than the opening longitudinal direction of vertical plate 9 Sectional area.
In the present invention, in specific implementation, the blower fan 10 should be installed through vertical plate 9, wherein, the blower fan 10 Air entry in the left side of the vertical plate 9, the gas outlet of the blower fan 10 is on the right side of the vertical plate 9.
In the present invention, in specific implementation, the longitudinal cross-section product of the left end entrance of the increaser 11 should be greater than vertical plate 9 The longitudinal cross-section product of central opening, the caliber of the low order end of the second air outlet 112 should be with the caliber of the Pneumatic conveying pipeline 1 It is identical.
Just a kind of work of regulatable new induction Pneumatic conveyer of particle concentration provided by the invention is former below Reason illustrates.
For the present invention, there are two kinds of working conditions can be selected according to the needs of user for it.
The first working condition:Naturally the working condition induced, now, the sliding panel 8 of the device are opened, and blower fan 10 stops Operation, its operation principle are:When air flows through reducing pipe 2, total head subtracts (i.e. parallel to distinguished and admirable, the pressure of face wind direction) Small, with the rise of wind speed, dynamic pressure (i.e. in the presence of blower fan, pressure caused by air flow) increases, and static pressure (air Molecule irregular movement and strike against caused pressure on tube wall) be reduced by, or even make static pressure subatmospheric power, because dynamic pressure Value added be transformed by static pressure, although (i.e. at the first air inlet 21) being to be in air-supply pipeline section at the mouth of pipe of reducing pipe 2 On, but the static pressure at this is negative value, then will suck air rather than extrude air ", now the first air outlet 22 of reducing pipe 2 The particulate in outside is inhaled into Mixed Zone due to negative pressure.It should be noted that the working condition induced naturally is applied to institute State the situation of the number concentration very little of particulate matter in gas in Pneumatic conveying pipeline 1;
It should be noted that the Mixed Zone refers to the Geldart-D particle between the right side of interseptal board 5 and the left side of vertical plate 9 The pipeline section region of pipeline (i.e. airduct) 1.The effect of Mixed Zone is primarily to make air-flow and the well-mixed region of particulate matter, more Required particle concentration is accurately attained, while also reduces part dynamic pressure, static pressure increase, steady air flow, air-flow is reduced and shakes It is dynamic, so as to reduce noise during particulate matter transmission.
It should also be noted that, the interseptal board 5 sets the first projection 51 and the second projection 53 in vertical direction, it is described First projection 51 and the second projection 53 are respectively designed to raised (for example, the front side wall of first projection 51 and described second convex Play 53 rear wall and the angle of vertical plane be respectively equal to 120 degree), it is therefore intended that prevent Mixed Zone from flow field dead angle occur, because If flow field dead angle, then to likely make that particulate matter can blow to dead angle area by air-flow, then be able to may reach Less than the required concentration of user, along with the current balance function of homogenating plate 6, with regard to can make that particulate matter mixes with air-flow more fully, Evenly, so as to reaching the number concentration of the particulate matter needed for user.
Second of working condition:Using mechanical induction working condition when, now, the blower fan 10 of the device and sliding panel 8 It is used in conjunction with each other, in the case that the air quantity, wind speed in the formation of blower fan 10 are fixed, is controlled by adjusting blower fan 10 with sliding panel 8 The size of negative pressure processed, meet user's needs so as to adjust the number concentration of particulate matter in gas in the Pneumatic conveying pipeline 1.Need It is noted that the number concentration of the working condition of mechanical induction particulate matter suitable for gas in the Pneumatic conveying pipeline 1 Bigger situation.
For the present invention, due to which employs reducing pipe 2, the interseptal board 5 of 4,120 degree of angles of swivel plate, V-type homogenating plate 6th, slideway 7, vertical plate 9, surrounding with the sliding panel 8 of rubber bar 80, blower fan 10, increaser 11 with dividing plate 111 etc. these Part, under the collective effect of these parts, allow whole Pneumatic conveyer in the process using gas transport particulate matter In, the number concentration of particulate matter in gas is adjusted according to the needs of user in real time, meets the user of different purposes in gas The varying number concentration necessary of particulate matter, and then the utilization rate of particulate matter is improved, and drastically increase its actual application Property.
For the present invention, it uses the induction principle of persuader, controllable so as to reach along with the mechanism of blower fan The effect of the number concentration of particulate matter in the gas of Pneumatic conveying pipeline, and then improve the purpose of the utilization rate of its particle.
Compared with prior art, the regulatable new induction Geldart-D particle dress of a kind of particle concentration provided by the invention Put, have the following technical effect that:
1st, design of the reducing pipe 2 in Pneumatic conveying pipeline 1 (i.e. airduct) is used, and is advantageous to make the of the right-hand member of reducing pipe 2 Static pressure subatmospheric power at one air outlet 22, so as to suck the particulate on the outside of the pipeline section of the first air outlet 22 of reducing pipe 2;
2nd, the design of swivel plate 4 is added at the pipeline section of the first air outlet 22 of reducing pipe 2, is advantageous to control air quantity and wind Speed;
3rd, the opening in interseptal board 5 using and 120 degree of the angle of vertical plane design, in the opening of interseptal board 5, favorably Enter Mixed Zone in guiding particulate, while the front side wall of first projection 51 and the rear wall of second projection 53 are with hanging down Mitre design (such as 120 degree) between facing directly, can prevent the generation at flow field dead angle in Mixed Zone;
4th, the design of the homogenating plate 6 of V-type, it is possible to reduce the generation of noise, while it is also beneficial to the uniformly mixed of air current composition Close;
5th, when using mechanical induction mode, the sliding panel 8 that blower fan 10 and surrounding carry rubber bar 80 is used in combination, can be with Control suction particulate number, so as to controlled concentration size;
6th, when starting blower fan 10 using mechanical induction mode, the rubber bar 80 on sliding panel 8 designs, and it is vertical to prevent The gas suction left side on the right side of plate 9;
7th, the increaser 11 with dividing plate 11 is used in outlet, is advantageous to part dynamic pressure to be changed into static pressure, it is so favourable In uniform air outlet wind speed and reduce noise;
8th, each part has the advantages of its protrusion and effect in the apparatus more than, there is its existing value and meaning, This induction Pneumatic conveyer provided by the invention is, it is necessary to which above all parts synergy, can just give full play to all parts The characteristics of, make whole Pneumatic conveyer that there is the controllable effect of concentration, and then the utilization ratio of particle is improved, and greatly Improve its actual application.
In summary, compared with prior art, the regulatable new induction of a kind of particle concentration provided by the invention Pneumatic conveyer, it can adjust gas according to the needs of user in real time during using gas transport particulate matter The number concentration of middle particulate matter, meet the user of different purposes to the varying number concentration necessary of particulate matter in gas, Jin Erti The utilization rate of high particulate matter, be advantageous to extensive popularization and application, be of great practical significance.
Described above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications also should It is considered as protection scope of the present invention.

Claims (10)

1. a kind of regulatable new induction Pneumatic conveyer of particle concentration, it is characterised in that including hollow pneumatic transporting Pipeline (1) is sent, the left and right ends of the Pneumatic conveying pipeline (1) are separately installed with reducing pipe (2) and increaser (11);
The left and right ends of the reducing pipe (2) have the first air inlet (21) and the first air outlet (22) respectively;
The left and right ends of the increaser (11) have the dividing plate (111) and the second air outlet (112) of central aperture respectively;
One swivel plate (4) is installed in first air outlet (22);
The inside top wall and bottom inside wall of the Pneumatic conveying pipeline (1) above the reducing pipe (2) respectively on One particulate generating means (3) is installed;
The madial wall of the Pneumatic conveying pipeline (1) is provided with one on the position corresponding with first air outlet (22) Interseptal board (5);
Positive the right of the interseptal board (5) is provided with a homogenating plate (6);
A vertical plate (9) is also equipped with the madial wall of the Pneumatic conveying pipeline (1);
The bottom of the vertical plate (9) is provided with a blower fan (10).
2. new induction Pneumatic conveyer as claimed in claim 1, it is characterised in that the top of first air inlet (21) Portion and the bottom inside top wall with the Pneumatic conveying pipeline (1) and the tangent connection of bottom inside wall respectively;
The top and bottom of second air outlet (112) the inside top wall with the Pneumatic conveying pipeline (1) and bottom respectively The tangent connection of portion's madial wall;
The swivel plate (4) is arranged on the vertical direction centre position of first air outlet (22).
3. new induction Pneumatic conveyer as claimed in claim 1, it is characterised in that particulate generating means (3) position Position between the interseptal board (5) and the first air inlet (21).
4. new induction Pneumatic conveyer as claimed in claim 1, it is characterised in that up and down the two of the vertical plate (9) End connects with the inside top wall and bottom inside wall of the Pneumatic conveying pipeline (1) respectively;
The vertical plate (9) is located at the right of the homogenating plate (6), and the vertical plate (9) is located at a positive left side for the dividing plate (111) Side.
5. the new induction Pneumatic conveyer as any one of Claims 1-4, it is characterised in that the vertical plate (9) upper right is provided with the slideway (7) of a vertical direction distribution, and a sliding panel is provided with the slideway (7) (8)。
6. new induction Pneumatic conveyer as claimed in claim 5, it is characterised in that first air inlet (21) is most left The bore at end is identical with the caliber of the Pneumatic conveying pipeline (1);
The bore of the first air inlet (21) of reducing pipe (2) left end from left to right progressively reduces, and the increaser (11) is right The bore of second air outlet (112) at end from left to right incrementally increases.
7. new induction Pneumatic conveyer as claimed in claim 5, it is characterised in that the interseptal board (5) is in Vertical Square First raised (51), compartment opening (52) and second raised (53) are distributed with upwards;
The front and rear sides inwall of the compartment opening (52) and the angle of vertical plane are equal to 120 degree;
The front side wall of described first raised (51) and the second raised rear wall of (53) and the angle of vertical plane are respectively equal to 120 degree.
8. new induction Pneumatic conveyer as claimed in claim 5, it is characterised in that the homogenating plate (6) is shaped as V Shape, the left end center of the homogenating plate (6) have tip (61), and the right-hand member of the homogenating plate (6) has both sides respectively up and down There is a plate tail (62), the vertical direction centre position of the tip (61) and the interseptal board (5) be located at same level highly On;
Horizontal range between the tip (61) and the plate tail (62) is the first air-out less than the reducing pipe (2) right-hand member The half of the bore of mouth (22).
9. new induction Pneumatic conveyer as claimed in claim 5, it is characterised in that the left side four of the sliding panel (8) Circumferential edges position is provided with rubber bar (80);
The air entry of the blower fan (10) is in the left side of the vertical plate (9), and the gas outlet of the blower fan (10) is described vertical The right side of plate (9).
10. new induction Pneumatic conveyer as claimed in claim 5, it is characterised in that the left end of the increaser (11) The longitudinal cross-section product of entrance is accumulated more than the longitudinal cross-section of the vertical plate (9) central opening, and second air outlet (112) is most right The caliber at end should be identical with the caliber of the Pneumatic conveying pipeline (1).
CN201710738478.8A 2017-08-25 2017-08-25 A kind of regulatable new induction Pneumatic conveyer of particle concentration Pending CN107352274A (en)

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CN109100271A (en) * 2018-09-26 2018-12-28 天津商业大学 A kind of air particle control technology comprehensive experiment table

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CH320983A (en) * 1952-12-24 1957-04-15 Miag Muehlenbau & Ind Gmbh Device for automatic regulation of the gas velocity in pipelines
GB756694A (en) * 1954-01-13 1956-09-05 Scottish Mechanical Light Ind Improvements in or relating to blower conveyors
CH320985A (en) * 1954-03-25 1957-04-15 Buehler Ag Geb Inlet device on pneumatic transport line
GB764441A (en) * 1955-01-21 1956-12-28 Simon Ltd Henry Improvements in pneumatic elevators for cereal grains and like materials
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CN85109727A (en) * 1985-01-04 1986-07-23 日本板硝子株式会社 Spraying apparatus for discharge of powder by pressed air
JPH04217513A (en) * 1990-07-24 1992-08-07 Kyowa Hakko Kogyo Co Ltd Pneumatic transfer system of solid material
CN2086246U (en) * 1990-08-11 1991-10-09 苏鹏 Stuff-suction device
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JPH09257235A (en) * 1996-03-21 1997-09-30 Mitsubishi Heavy Ind Ltd Flow rate regulator for powdered body transport pipe
CN1235865A (en) * 1998-05-15 1999-11-24 中国石油化工总公司 Method and device for realizing circulation fluidized bed multistage operation by using tube wall air compensation and air exhaustion
US20030150928A1 (en) * 2000-01-27 2003-08-14 Yasushi Watanabe Constant volume delivery device and method of delivering powder material
CN1458899A (en) * 2000-09-18 2003-11-26 保尔·沃特公司 Device for passing heaving flowing bulk material into delivery pipe
CN2461902Y (en) * 2001-02-16 2001-11-28 吴多民 Non-air hose aluminium oxide super-thick phase conveyer
CN1509391A (en) * 2001-03-23 2004-06-30 �����Ӳ��������������ι�˾ Method and apparatus for setting air ratio
CN1518654A (en) * 2001-12-03 2004-08-04 �Ͳ�����������ʽ���� Fuel distribution device for fuel feed ducts, and fuel supply device with the fuel distribution device
JP2004037329A (en) * 2002-07-05 2004-02-05 Matsui Mfg Co Metering device of powder granular material
CN1778997A (en) * 2004-11-25 2006-05-31 贵阳铝镁设计研究院 Impurities removing method and apparatus for ultra-concentrated aluminium oxide transferring system
CN2771151Y (en) * 2004-12-03 2006-04-12 镇江市电站辅机厂 Concentration regulating device
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EP2213377A1 (en) * 2007-11-30 2010-08-04 Mitsubishi Heavy Industries, Ltd. Powder separation device and solid-fuel burner
CN102105370A (en) * 2008-07-24 2011-06-22 马丁工程公司 Air cannon for removal of flowable material from a material handling system
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CN202098861U (en) * 2011-06-03 2012-01-04 大庆科美达采油成套设备有限公司 Wind-driven dry powder conveyor for preparing polymer injection liquid
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CN103029990A (en) * 2011-10-03 2013-04-10 通用电气公司 System and method for transporting solid feed in a solid feed pump
CN202369126U (en) * 2011-12-19 2012-08-08 贵阳铝镁设计研究院有限公司 Material speed reducing and flow limiting device
CN202732432U (en) * 2012-09-10 2013-02-13 中国能源建设集团广东省电力设计研究院 Bypass air flue control loop used for preventing vibration of low load of thermal power plant axial flow fan
CN103395627A (en) * 2013-07-12 2013-11-20 裕东(中山)机械工程有限公司 Coaxial pneumatic conveying ejector
CN104670749A (en) * 2013-12-03 2015-06-03 赵颖奇 Multifunctional blood storage and transportation container
CN103954063A (en) * 2014-04-24 2014-07-30 华南理工大学 Refrigerating system with single-valve stepless adjustment of circulating concentration of mixed working medium and method thereof
CN106715358A (en) * 2014-06-05 2017-05-24 宾德公司 Method for expanding raw material in the form of sand grains
CN104444380A (en) * 2014-11-19 2015-03-25 燕山大学 Negative pressure pneumatic conveying type rotary feeder
CN105059944A (en) * 2015-08-14 2015-11-18 北京华清茵蓝科技有限公司 Pneumatic conveying powder flowing speed adjusting device with adjustable double side baffle plates
CN105712084A (en) * 2016-02-01 2016-06-29 北京理工大学 Gas pressure-driven type even powder supply device and method
CN105966921A (en) * 2016-07-20 2016-09-28 苏州中材建设有限公司 Material issuing device for powdered solid and gas conveying
CN205855389U (en) * 2016-07-28 2017-01-04 长沙永阳环保科技有限公司 A kind of efficient cyclone nozzle for powder injection pump
CN106315230A (en) * 2016-11-07 2017-01-11 中国石油大学(华东) Experimental multifunctional negative-pressure powder material feeder
CN106829227A (en) * 2017-04-13 2017-06-13 李福军 The fine quantification accumulating conveying device of powder and its method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109100271A (en) * 2018-09-26 2018-12-28 天津商业大学 A kind of air particle control technology comprehensive experiment table

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