CN205413269U - A reducing mechanism for bolognian stone - Google Patents

A reducing mechanism for bolognian stone Download PDF

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Publication number
CN205413269U
CN205413269U CN201521042868.4U CN201521042868U CN205413269U CN 205413269 U CN205413269 U CN 205413269U CN 201521042868 U CN201521042868 U CN 201521042868U CN 205413269 U CN205413269 U CN 205413269U
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CN
China
Prior art keywords
cavity
isolated chambers
barite
granule
material pipe
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201521042868.4U
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Chinese (zh)
Inventor
谭光英
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Chongqing Bawang Minerals Co ltd
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Chongqing Bawang Minerals Co ltd
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Priority to CN201521042868.4U priority Critical patent/CN205413269U/en
Application granted granted Critical
Publication of CN205413269U publication Critical patent/CN205413269U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a reducing mechanism for bolognian stone, including crocus cavity and sieve material pipe, there is the isolation cavity at crocus cavity internal fixation, keep apart vertically in the cavity being provided with a plurality of support columns, rotate on the support column and be provided with outer axle, outer epaxially articulatedly have a plurality of cutting pieces, has offered the supply -air outlet on crocus cavity outer wall, is provided with the ventilation holes who corresponds with the supply -air outlet on keeping apart the cavity, arranges material pipe one end and runs through the middle part of crocus cavity and extend to sieve material outside of tubes, arranges to expect to manage the other end and install and draw from the fan, at the terminal one end intercommunication through bleeder valve and passage of row material pipe, the other end and the hopper intercommunication of passage are installed on the passage and are pull the fan. When bolognian stone granule and granule bumped, the airflow flow velocity in the ventilation holes was great, and ventilation holes slope simultaneously sets up for the bolognian stone granule hardly enters into the annular space through ventilation holes, avoids removing the formation whirl and causing the hindrance gas, improves the crushing efficiency of bolognian stone granule.

Description

A kind of reducing mechanism for barite
Technical field
This utility model relates to Ore polish field, specifically refers to a kind of reducing mechanism for barite.
Background technology
Barite belongs to non-renewable resources, is one of Chinese trump-cards in the export of mineral products, is widely used in oil, the heavy weight additive of natural gas drilling mud, and the consumption figure in fields such as barium chemical industry, fillers is also increasing year by year.China's barite resources is the abundantest, is distributed in 21 provinces in the whole nation, 3.6 hundred million tons of total reserves Ore, occupies the 1st, the world.Medically can be used for contrast agent in digestive system.
During actually used, generally use disintegrating machine to realize barite to pulverize to form barite raw material, but in prior art, the pulverizing of barite particle is easy to occur that granular size differs, and coarse fodder is difficult with the collection of fines, needing the most further to be screened, crushing efficiency is low and causes production cost and labour cost higher.
Utility model content
The purpose of this utility model is to provide a kind of reducing mechanism for barite, to overcome the problems referred to above.
The purpose of this utility model is achieved through the following technical solutions:
A kind of reducing mechanism for barite, including the pulverizing cavity being interconnected and sieve material pipe, the isolated chambers of annular it is fixed with in described pulverizing cavity, described isolated chambers and pulverizing cavity annular space, multiple support column it is vertically arranged with in isolated chambers, rotate on support column and be provided with outer shaft, multiple cutting sheet it is hinged with on outer shaft, pulverizing chamber outer wall offers the air outlet connected with described annular space, the wind pushing hole corresponding with air outlet it is provided with in described isolated chambers, the axes intersect of the axis of described wind pushing hole and described isolated chambers and out of plumb, also include drainage conduit and hopper, described hopper connects with isolated chambers, described drainage conduit one end is run through the middle part of pulverizing cavity and extends outside sieve material pipe, the drainage conduit other end extends outside pulverizing cavity and is provided with at this end and deflects from blower fan;Being connected with one end of passage by outlet valve at described drainage conduit end, the other end of passage connects with hopper, and is provided with traction blower fan on passage.
During utility model works, in annular space, swiftly flowing gas is injected by air outlet, after gas is by doing certain circular motion in annular space, entered in isolated chambers by wind pushing hole, due to the axis of wind pushing hole and the axes intersect of isolated chambers but out of plumb, i.e. wind pushing hole is obliquely installed, and constantly enters into the gas in isolated chambers and forms eddy flow;Now the barite particle after first grinding enters in isolated chambers by hopper, granule mixes with eddy flow, make mutually to collide between the granule of different size size, under the influence of active force with counteracting force, partial particulate is launched to isolated chambers inwall after collision occurs, and is re-introduced in eddy flow through reflection, i.e. carries out collision repeatedly, make larger-diameter granule gradually become fine particle, eventually form superfines;And along with the movement of eddy flow, the bigger granule of section diameter is under its action of gravity, the granule of this part directly drops to the end of drainage conduit, and ultra-fine powder is then discharged by drainage conduit upper end under the absorption deflecting from blower fan is drawn, and then realizes the extra-fine grinding operation of barite.When barite particle collides with granule, air-flow velocity in wind pushing hole is relatively big, and wind pushing hole is obliquely installed simultaneously so that barite particle is difficult to enter in annular space by wind pushing hole, avoid gas moving formation eddy flow and causing obstruction, improve the crushing efficiency of barite particle.
Wherein, under the effect of eddy flow, the outer shaft on support column can be driven to rotate, and then drive cutting sheet to rotate, so, bigger barite particle can be cut;Meanwhile, eddy flow also can make granule directly impinge upon on outer shaft, and turns to outer shaft into row stochastic restriction, so, can constantly change turning to of cutting sheet, to strengthen the crushing effect to granule.When the tenesmus of part larger particles is to drainage conduit end, open outlet valve, bigger granule is re-moved to hopper by passage under the drive of traction blower fan, broken with carry out again, and then form the circulation line that a barite particle crushes repeatedly, i.e. ensure that the diameter of the barite particle discharged by discharge nozzle upper end reaches ultra-fine standard, improve the super fine crushing efficiency of barite further.
Further, the end internal diameter of described sieve material pipe successively decreases downwards along its axis.Larger-diameter granule also suffers from the Effect of Rotation of eddy flow when tenesmus and continues to collide with sieve material inside pipe wall, i.e. constantly rebound on sieve material inside pipe wall, and be arranged to successively decrease downwards along its axis by the end internal diameter of sieve material pipe, reducing is formed at sieve material pipe end, reduce the rebound rate of major diameter granule, accelerate the collection of major diameter granule.
Further, also including feed pipe, described hopper is connected with described isolated chambers by feed pipe.So, the charging of barite particle in isolated chambers can be avoided uneven, and then prevent from reducing crushing efficiency.
Further, the blast pipe connected with described feed pipe is also included.In feed pipe, injected the pusher air-flow of auxiliary by blast pipe, blocking occurs in can preventing feed pipe, accelerates the collision frequency between isolated chambers endoparticle and granule simultaneously, improve the super fine crushing efficiency of barite further.
This utility model compared with prior art, has such advantages as and beneficial effect:
1, this utility model is when barite particle collides with granule, air-flow velocity in wind pushing hole is bigger, wind pushing hole is obliquely installed simultaneously, barite particle is made to be difficult to enter in annular space by wind pushing hole, avoid gas moving formation eddy flow and causing obstruction, improve the crushing efficiency of barite particle.
2, the end internal diameter of sieve material pipe is arranged to successively decrease downwards along its axis by this utility model, forms reducing at sieve material pipe end, reduces the rebound rate of major diameter granule, accelerate the collection of major diameter granule.
3, during this utility model application, under the effect of eddy flow, the cutting sheet being arranged on outer shaft can be driven to rotate, so, bigger barite particle can be cut;Meanwhile, eddy flow also can make granule directly impinge upon on outer shaft, and constantly change cutting sheet turn to strengthen crushing effect to granule.
4, hopper is connected with isolated chambers by feed pipe, so, the charging of barite particle in isolated chambers can be avoided uneven, and then prevent reduction crushing efficiency.
5, in feed pipe, injected the pusher air-flow of auxiliary by blast pipe, in feed pipe can be prevented, blocking occurs;Meanwhile, accelerate the collision frequency between isolated chambers endoparticle and granule, improve the super fine crushing efficiency of barite further.
6, during this utility model application, bigger granule is re-moved to hopper by passage under the drive of traction blower fan, broken with carry out again, and then form the circulation line that a barite particle crushes repeatedly, i.e. ensure that the diameter of the barite particle discharged by discharge nozzle upper end reaches ultra-fine standard, improve the super fine crushing efficiency of barite further.
Accompanying drawing explanation
Accompanying drawing described herein is used for providing being further appreciated by this utility model embodiment, constitutes the part of the application, is not intended that the restriction to this utility model embodiment.In the accompanying drawings:
Fig. 1 is the structural representation of a kind of one specific embodiment of reducing mechanism for barite described in the utility model;
Fig. 2 is a kind of structural representation of one specific embodiment of outer shaft in the reducing mechanism of barite described in the utility model.
Labelling and corresponding parts title in accompanying drawing: 1, hopper, 2, blast pipe, 3, feed pipe, 4, air outlet, 5, wind pushing hole, 6, deflect from blower fan, 7, drainage conduit, 8, pulverizing cavity, 9, isolated chambers, 10, sieve material pipe, 11, outlet valve, 12, passage, 13, traction blower fan, 14, support column, 15, outer shaft, 16, cutting sheet.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, exemplary embodiment of the present utility model and explanation thereof are only used for explaining this utility model, are not intended as restriction of the present utility model.
Embodiment 1
As shown in Figure 1 to Figure 2, the present embodiment includes pulverizing cavity 8 and the sieve material pipe 10 being interconnected, the isolated chambers 9 of annular it is fixed with in described pulverizing cavity 8, described isolated chambers 9 and pulverizing cavity 8 annular space, multiple support column 14 it is vertically arranged with in isolated chambers 9, rotate on support column 14 and be provided with outer shaft 15, outer shaft 15 is hinged with multiple cutting sheet 16;Pulverizing cavity 8 outer wall offers the air outlet 4 connected with described annular space, described isolated chambers 9 is provided with axes intersect and the out of plumb of the wind pushing hole 5 corresponding with air outlet 4, the axis of described wind pushing hole 5 and described isolated chambers 9;Also including that drainage conduit 7 and hopper 1, described hopper 1 connect with isolated chambers 9, described drainage conduit 7 one end is run through the middle part of pulverizing cavity 8 and extends outside sieve material pipe 10, and drainage conduit 7 other end extends outside pulverizing cavity 8 and is provided with at this end and deflects from blower fan 6;Being connected with one end of passage 12 by outlet valve 11 at described sieve material pipe 10 end, the other end of passage 12 connects with hopper 1, and is provided with traction blower fan 13 on passage 12.
During work, in annular space, swiftly flowing gas is injected by air outlet 4, after gas is by doing certain circular motion in annular space, entered in isolated chambers 9 by wind pushing hole 5, due to the axis of wind pushing hole 5 and the axes intersect of isolated chambers 9 but out of plumb, i.e. wind pushing hole 5 is obliquely installed, and constantly enters into the gas in isolated chambers 9 and forms eddy flow;Now the barite particle after first grinding enters in isolated chambers 9 by hopper 1, granule mixes with eddy flow, make mutually to collide between the granule of different size size, under the influence of active force with counteracting force, partial particulate is launched to isolated chambers 9 inwall after collision occurs, and is re-introduced in eddy flow through reflection, i.e. carries out collision repeatedly, make larger-diameter granule gradually become fine particle, eventually form superfines;And along with the movement of eddy flow, the bigger granule of section diameter is under its action of gravity, the granule of this part directly drops to the end of drainage conduit 7, and ultra-fine powder is then discharged by drainage conduit 7 upper end under the absorption deflecting from blower fan 6 is drawn, and then realizes the extra-fine grinding operation of barite.When barite particle collides with granule, air-flow velocity in wind pushing hole 5 is relatively big, and wind pushing hole 5 is obliquely installed simultaneously so that barite particle is difficult to enter in annular space by wind pushing hole 5, avoid gas moving formation eddy flow and causing obstruction, improve the crushing efficiency of barite particle.
Wherein, under the effect of eddy flow, the outer shaft 15 on support column 14 can be driven to rotate, and then drive cutting sheet 16 to rotate, so, bigger barite particle can be cut;Meanwhile, eddy flow also can make granule directly impinge upon on outer shaft 15, and turns to into row stochastic restriction to outer shaft 15, so, can constantly change turning to of cutting sheet 16, to strengthen the crushing effect to granule.When the tenesmus of part larger particles is to drainage conduit 7 end, open outlet valve 11, bigger granule is re-moved to hopper 1 by passage 12 under the drive of traction blower fan 13, broken with carry out again, and then form the circulation line that a barite particle crushes repeatedly, i.e. ensure that the diameter of the barite particle discharged by drainage conduit 7 upper end reaches ultra-fine standard, improve the super fine crushing efficiency of barite further.
As preferably, the end internal diameter of described sieve material pipe 10 successively decreases downwards along its axis.Larger-diameter granule also suffers from the Effect of Rotation of eddy flow when tenesmus and continues to collide with sieve material pipe 10 inwall, i.e. constantly rebound on sieve material pipe 10 inwall, and be arranged to successively decrease downwards along its axis by the end internal diameter of sieve material pipe 10, reducing is formed at sieve material pipe 10 end, reduce the rebound rate of major diameter granule, accelerate the collection of major diameter granule.
Preferably, also include that feed pipe 3, described hopper 1 are connected with described isolated chambers 9 by feed pipe 3.So, in can avoiding isolated chambers 9, barite particle charging is uneven, and then prevents from reducing crushing efficiency.
Preferably, the blast pipe 2 connected with described feed pipe 3 is also included.In feed pipe 3, injected the pusher air-flow of auxiliary by blast pipe 2, blocking occurs in can preventing feed pipe 3, accelerates the collision frequency between isolated chambers 9 endoparticle and granule simultaneously, improve the super fine crushing efficiency of barite further.
Above-described detailed description of the invention; the purpose of this utility model, technical scheme and beneficial effect are further described; it is it should be understood that; the foregoing is only detailed description of the invention of the present utility model; it is not used to limit protection domain of the present utility model; all within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. done, within should be included in protection domain of the present utility model.

Claims (4)

1. the reducing mechanism for barite, including the pulverizing cavity (8) being interconnected and sieve material pipe (10), it is characterized in that: in described pulverizing cavity (8), be fixed with the isolated chambers (9) of annular, described isolated chambers (9) and pulverizing cavity (8) annular space, multiple support column (14) it is vertically arranged with in isolated chambers (9), the upper rotation of support column (14) is provided with outer shaft (15), and outer shaft (15) is hinged with multiple cutting sheet (16);Pulverizing cavity (8) outer wall offers the air outlet (4) connected with described annular space, axes intersect and the out of plumb of the wind pushing hole (5) corresponding with air outlet (4), the axis of described wind pushing hole (5) and described isolated chambers (9) it is provided with in described isolated chambers (9);Also include drainage conduit (7) and hopper (1), described hopper (1) connects with isolated chambers (9), described drainage conduit (7) one end is run through the middle part of pulverizing cavity (8) and extends to sieve material pipe (10), and drainage conduit (7) other end extends outward to pulverizing cavity (8) and is provided with at this end and deflects from blower fan (6);Connected with one end of passage (12) by outlet valve (11) at described sieve material pipe (10) end, the other end of passage (12) connects with hopper (1), and is provided with traction blower fan (13) on passage (12).
A kind of reducing mechanism for barite the most according to claim 1, it is characterised in that: the end internal diameter of described sieve material pipe (10) successively decreases downwards along its axis.
A kind of reducing mechanism for barite the most according to claim 1, it is characterised in that: also including feed pipe (3), described hopper (1) is connected with described isolated chambers (9) by feed pipe (3).
A kind of reducing mechanism for barite the most according to claim 3, it is characterised in that: also include the blast pipe (2) connected with described feed pipe (3).
CN201521042868.4U 2015-12-15 2015-12-15 A reducing mechanism for bolognian stone Expired - Fee Related CN205413269U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201521042868.4U CN205413269U (en) 2015-12-15 2015-12-15 A reducing mechanism for bolognian stone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201521042868.4U CN205413269U (en) 2015-12-15 2015-12-15 A reducing mechanism for bolognian stone

Publications (1)

Publication Number Publication Date
CN205413269U true CN205413269U (en) 2016-08-03

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CN201521042868.4U Expired - Fee Related CN205413269U (en) 2015-12-15 2015-12-15 A reducing mechanism for bolognian stone

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107442246A (en) * 2017-07-27 2017-12-08 贵州宏鑫超微新材料有限公司 Barite disruption elements and process units

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107442246A (en) * 2017-07-27 2017-12-08 贵州宏鑫超微新材料有限公司 Barite disruption elements and process units
CN107442246B (en) * 2017-07-27 2019-03-01 贵州宏鑫超微新材料有限公司 Barite disruption elements and process units

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160803

Termination date: 20161215

CF01 Termination of patent right due to non-payment of annual fee