CN207970990U - A kind of double tapered angle rotary drum - Google Patents

A kind of double tapered angle rotary drum Download PDF

Info

Publication number
CN207970990U
CN207970990U CN201721904701.3U CN201721904701U CN207970990U CN 207970990 U CN207970990 U CN 207970990U CN 201721904701 U CN201721904701 U CN 201721904701U CN 207970990 U CN207970990 U CN 207970990U
Authority
CN
China
Prior art keywords
cone
rotary drum
angle rotary
section
cone section
Prior art date
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.)
Active
Application number
CN201721904701.3U
Other languages
Chinese (zh)
Inventor
李振威
黄滨
李强
张修全
许珊珊
陈勇光
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Haishen Machinery & Electronics General Works (xiangshan)
Heilongjiang Lande Unltrasound Technology Co Ltd
Original Assignee
Haishen Machinery & Electronics General Works (xiangshan)
Heilongjiang Lande Unltrasound Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Haishen Machinery & Electronics General Works (xiangshan), Heilongjiang Lande Unltrasound Technology Co Ltd filed Critical Haishen Machinery & Electronics General Works (xiangshan)
Priority to CN201721904701.3U priority Critical patent/CN207970990U/en
Application granted granted Critical
Publication of CN207970990U publication Critical patent/CN207970990U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Centrifugal Separators (AREA)

Abstract

A kind of double tapered angle rotary drum of the utility model can enhance solid phase drying, be conducive to the discharge of high viscosity solid phase, for being separated by solid-liquid separation.Hollow rotating shaft is rotatably connected on the inside of cone angle rotary drum, cone angle rotary drum and hollow rotating shaft are coaxial, spiral transmitter is fixed on hollow rotating shaft, BD plates are fixed on hollow rotating shaft, space between cone angle rotary drum and hollow rotating shaft is divided into left chamber body and right chamber body, there are spacing, unidirectional filter device to be arranged on BD plates between the outer end face and the inner surface of cone angle rotary drum of BD plates, filter device is located at right chamber body end, and solid-phase outlet is located at left chamber body end;Cone angle rotary drum is respectively to bore section I, cone section II, cone section III, cone section IV and cone section V from left end toward right end, and solid-phase outlet setting is in cone section I, and filter device setting is in cone section V;Feed inlet and outlet, feed inlet and outlet are provided on hollow rotating shaft, feed inlet is located at one end of hollow rotating shaft, and outlet is positioned at the inside of cone angle rotary drum and in right chamber body.

Description

A kind of double tapered angle rotary drum
Technical field
The utility model is related to a kind of rotary drums, are in particular a kind of double tapered angle rotary drums.
Background technology
Rotary drum is a kind of equipment for separating liquid from solid being industrially commonly used, and the practicality of Patent No. 201420667704.X is new Type patent discloses a kind of double tapered angle drum structure of decanter centrifuge, it includes rotary drum shell (1), is set in rotary drum shell (1) It includes front end shell (101) and rear piece housing (102), front end shell (101) to have screw feeder (2), the rotary drum shell (1) Angle is formed between rear piece housing (102), it is characterised in that:The preceding piece housing (101) is cone tubular shell, the back segment Shell (102) is cone tubular shell, and the cone angle of the rear piece housing (102) is more than the cone angle of preceding piece housing (101).The practicality is new Type efficiently utilizes the effect of centrifugal force, and resultant force is collectively formed in the effect with spiral pusher, and solid is made to be more advantageous to discharge, can Effectively to solve the problems, such as that the wet and slippery material of solid is difficult to be detached with existing decanter centrifuge, in bio-pharmaceuticals, food processing row Industry is with a wide range of applications.But the rotary drum shell in the utility model is only single taper, and high viscosity solid phase is discharged Improvement is smaller.In addition, the pressure having no idea using liquid, pushes the discharge of high viscosity solid phase.
Utility model content
The utility model can enhance solid phase drying, have mainly solving the technical problems that provide a kind of double tapered angle rotary drum It is discharged conducive to high viscosity solid phase.
In order to solve the above technical problems, a kind of double tapered angle rotary drum of the utility model is turned by cone angle rotary drum, hollow rotating shaft, spiral Device, BD plates, unidirectional filter device, filter device and solid-phase outlet composition are sent, solid phase drying can be enhanced, it is solid to be conducive to high viscosity Mutually it is discharged.
The hollow rotating shaft is rotatably connected on the inside of the cone angle rotary drum, and the cone angle rotary drum and hollow rotating shaft are coaxial, The spiral transmitter is fixed on the hollow rotating shaft, and the BD plates are annular slab and are fixed on the hollow rotating shaft, institute State BD plates and the space between cone angle rotary drum and hollow rotating shaft be divided into left chamber body and right chamber body, the outer end face of the BD plates with it is described There are spacing between the inner surface of cone angle rotary drum, the unidirectional filter device is arranged on the BD plates, the filter device and Solid-phase outlet is separately positioned on the both ends of the cone angle rotary drum, and the filter device is located at right chamber body end, the solid-phase outlet position In left chamber body end;
The cone angle rotary drum is made of cone section I, cone section II, cone section III, cone section IV and cone section V, and the cone angle rotary drum is from a left side It is respectively to bore section I, cone section II, cone section III, cone section IV and cone section V, the solid-phase outlet to be arranged in the cone section I to hold toward right end On, the filter device is arranged in the cone section V;
Feed inlet and outlet, the feed inlet and outlet are provided on the hollow rotating shaft, the feed inlet is located at One end of the hollow rotating shaft, the outlet is positioned at the inside of the cone angle rotary drum and in right chamber body.
As advanced optimizing for the utility model, the cone section I described in a kind of double tapered angle rotary drum of the utility model and cone section III is parallel-segment, and the cone section II, cone section IV and cone section V are tilting section, and the cone section II tilts outward, the cone section II left end is small end, and the right end of the cone section II is big end, and the cone section IV and cone section V tilt and bore section V inwardly Angle of inclination is more than cone section IV, and the cone section IV and the left end for boring section V are big end, and the cone section IV and the right end for boring section V are Small end.
As advanced optimizing for the utility model, the outer end face of the BD plates described in a kind of double tapered angle rotary drum of the utility model Parallel with the cone section III, spacing between the two is 2-3mm, and cavity tilts the BD plates to the left.
As advanced optimizing for the utility model, the unidirectional filter device described in a kind of double tapered angle rotary drum of the utility model For porous ceramics so that only liquid can flow to right chamber body from left chamber body by unidirectional filter device.
As advanced optimizing for the utility model, the filter device described in a kind of double tapered angle rotary drum of the utility model is more Hole is ceramic, and the liquid for being discharged in right chamber body simultaneously prevents solid from being discharged.
As advanced optimizing for the utility model, the cone angle rotary drum described in a kind of double tapered angle rotary drum of the utility model and sky The junction of heart shaft is provided with sealing device.
A kind of double tapered angle rotary drum of the utility model has the beneficial effect that:
1. being provided with multistage cone section on cone angle rotary drum, solid phase drying can be enhanced, be conducive to the discharge of high viscosity solid phase.
2. being provided with BD plates, can have and squeeze solid phase using fluid pressure, solid phase drying can be enhanced, it is solid to be conducive to high viscosity Mutually it is discharged.
Description of the drawings
The utility model is described in more detail with specific implementation method below in conjunction with the accompanying drawings.
Fig. 1 is a kind of structural schematic diagram of double tapered angle rotary drum of the utility model.
In figure:Cone angle rotary drum 1;Bore I 1-1 of section;Bore II 1-2 of section;Bore III 1-3 of section;Bore IV 1-4 of section;Bore V 1-5 of section;It is hollow Shaft 2;Feed inlet 2-1;Export 2-2;Spiral transmitter 3;BD plates 4;Unidirectional filter device 5;Filter device 6;Solid-phase outlet 7.
Specific implementation mode
Illustrate that present embodiment, a kind of double tapered angle rotary drum of the utility model can enhance solid phase drying with reference to Fig. 1, Be conducive to the discharge of high viscosity solid phase.
The double tapered angle rotary drum is by cone angle rotary drum 1, hollow rotating shaft 2, spiral transmitter 3, BD plates 4, unidirectional filter device 5, mistake It filters device 6 and solid-phase outlet 7 forms, the hollow rotating shaft 2 is rotatably connected on the inside of the cone angle rotary drum 1, and the cone angle turns Drum 1 and hollow rotating shaft 2 are coaxial, and the speed that hollow rotating shaft 2 rotates is less than the speed that cone angle rotary drum 1 rotates.The spiral transmitter 3 It is fixed on the hollow rotating shaft 2, is followed by hollow rotating shaft 2 and rotates together.Spiral transmitter 3 is during rotation by solid phase Constantly pushed toward solid-phase outlet 7.The BD plates 4 are annular slab and to be fixed on the hollow rotating shaft 2, and the BD plates 4 are by cone angle Space between rotary drum 1 and hollow rotating shaft 2 is divided into left chamber body and right chamber body, the outer end face of the BD plates 4 and the cone angle rotary drum 1 Inner surface between there are spacing, this spacing to pass through for solid phase.The unidirectional filter device 5 is arranged on the BD plates 4, institute It states filter device 6 and solid-phase outlet 7 is separately positioned on the both ends of the cone angle rotary drum 1, the filter device 6 is located at right chamber body End, the solid-phase outlet 7 are located at left chamber body end;Unidirectional filter device 5 allows the liquid in left chamber body to lead to right chamber body, and Liquid in right chamber body cannot lead to left chamber body, and solid phase can not pass through from unidirectional filter device 5.Filter device 6 is used for Excessive liquid in right chamber body is discharged, when the liquid in right chamber body is continuously increased will be from filter device 6 more than filter device 6 Middle discharge.Solid-phase outlet 7 is for solid phase to be discharged from left chamber body.
The cone angle rotary drum 1 is made of I 1-1 of cone section, II 1-2 of cone section, III 1-3 of cone section, cone IV 1-4 of section and cone V 1-5 of section, The cone angle rotary drum 1 is respectively to bore I 1-1 of section, II 1-2 of cone section, III 1-3 of cone section, cone IV 1-4 of section and cone section V from left end toward right end 1-5, the solid-phase outlet 7 are arranged on I 1-1 of cone section, and the filter device 6 is arranged on V 1-5 of cone section;
It is provided with feed inlet 2-1 on the hollow rotating shaft 2 and outlet 2-2, the feed inlet 2-1 are connected to outlet 2-2, institute One end that feed inlet 2-1 is located at the hollow rotating shaft 2 is stated, the outlet 2-2 is located at the inside of the cone angle rotary drum 1 and positioned at the right side In cavity.Solid-liquid batch mixing enters 2 inside of hollow rotating shaft from feed inlet 2-1 and enters in right chamber body from outlet 2-2.Due to hollow turn 1 high-speed rotation of axis 2 and cone angle rotary drum, under the influence of centrifugal force, the big solid phase particles of density, which are got rid of, to be attached in cone angle rotary drum 1 Surface forms solid circular layer, and the smaller liquid of density can only form pendular ring layer since centrifugal force is smaller in the inside of solid circular layer.
I 1-1 of cone section and III 1-3 of cone section is parallel-segment, II 1-2 of cone section, cone IV 1-4 of section and V 1- of cone section 5 be tilting section, and II 1-2 of cone section is tilted outward, and the left end of II 1-2 of the cone section is small end, the right side of II 1-2 of the cone section It is big end to hold, and cone IV 1-4 of section and cone V 1-5 of section are tilted and bored the angle of inclination of V 1-5 of section more than IV 1- of cone section inwardly 4, cone IV 1-4 of section and the left end for boring V 1-5 of section are big end, and cone IV 1-4 of section and the right end for boring V 1-5 of section are small end. The inclined direction and angle for boring V 1-5 of IV 1-4 of section and cone section move convenient for solid phase to solid-phase outlet 7.I 1-1 of section is bored convenient for discharge Solid phase.
The outer end face of the BD plates 4 is parallel with cone III 1-3 of section, and spacing between the two is 2-3mm, the BD plates 4 cavity inclinations to the left.Spacing between III 1-3 of 4 outer end face of BD plates and cone section leads to left chamber body for solid phase from right chamber body, simultaneously Solid phase is squeezed, the content liquid in solid phase is reduced.When spacing is excessive, extruding solid phase is not just had, reduces liquid in solid phase The effect of content is unfavorable for solid phase discharge when spacing is too small.
The cavity inclination to the left of BD plates 4 leads to left chamber body convenient for solid phase from right chamber body.
The unidirectional filter device 5 is porous ceramics so that only liquid can pass through unidirectional filter device 5 from left chamber body Right chamber body is flowed to, and liquid cannot flow to left chamber body from right chamber body by unidirectional filter device 5.In addition, solid phase can not pass through Unidirectional filter device 5.
The filter device 6 is porous ceramics, and the liquid for being discharged in right chamber body simultaneously prevents solid from being discharged.
The junction of the cone angle rotary drum 1 and hollow rotating shaft 2 is provided with sealing device, prevents liquid or solid from cone angle Rotary drum 1 and the junction of hollow rotating shaft 2 leak out.
The operation principle of the utility model is:
Cone angle rotary drum 1 turns to identical with hollow rotating shaft 2, and 2 rotating ratio cone angle rotary drum 1 of hollow rotating shaft is low, when solid-liquid batch mixing Enter 2 inside of hollow rotating shaft from feed inlet 2-1 and enters in right chamber body from outlet 2-2.Due to hollow rotating shaft 2 and cone angle rotary drum 1 High-speed rotation, under the influence of centrifugal force, the big solid phase particles of density are got rid of the inner surface for being attached to cone angle rotary drum 1, form solid ring Layer, the smaller liquid of density can only form pendular ring layer since centrifugal force is smaller in the inside of solid circular layer.Due to cone angle rotary drum 1 with The rotating speed of hollow rotating shaft 2 is different, and there are relative motions, i.e. speed discrepancy, i.e. both cone angle rotary drum 1 and spiral transmitter 3 to deposit for the two In relative motion.Using the relative motion between cone angle rotary drum 1 and spiral transmitter 3, solid circular layer is slowly pushed to solid phase Outlet 7 is simultaneously discharged from solid-phase outlet 7.
In the process, the liquid in right chamber body can be more and more, and liquid in right chamber body can be controlled by filter device 6 Amount, excessive liquid is discharged from right chamber body.When the amount of liquid in right chamber body increases, liquid can squeeze solid circular layer, add The solid circular layer of speed enters 7 row of solid-phase outlet along cone V 1-5 of section, IV 1-4 of cone section, III 1-3 of cone section, cone II 1-2 of section and cone I 1-1 of section Go out.It bores V 1-5 of section, cone IV 1-4 of section and bores the setting in II angles of inclination 1-2 of section and direction and be discharged convenient for solid phase.4 outer end face of BD plates Spacing between cone III 1-3 of section can make solid phase lead to left chamber body from right chamber body, while squeeze solid phase, by the liquid in solid phase Body content reduces, and is discharged convenient for solid phase.The cavity inclination to the left of BD plates 4 also allows for solid phase and leads to left chamber body from right chamber body.
When the liquid in left chamber body is more and more, will be entered in right chamber body by unidirectional filter device 5, to squeeze Solid phase in right chamber body is moved toward solid-phase outlet 7.Additionally due to cone II 1-2 of section is tilted outward, the space of left chamber body from it is right toward It is left smaller and smaller so that Gu the extruding force that circular layer is subject to is increasing, Gu the liquid in circular layer is pressed further by discharge, to increase The drying of solid circular layer is conducive to the discharge of high viscosity solid phase.
Certainly, above description is not limitation of the utility model, and the utility model is also not limited to the example above, this skill The variations, modifications, additions or substitutions that the those of ordinary skill in art field is made in the essential scope of the utility model, also belong to In the scope of protection of the utility model.

Claims (6)

1. a kind of double tapered angle rotary drum, it is characterised in that:The double tapered angle rotary drum is turned by cone angle rotary drum (1), hollow rotating shaft (2), spiral Send device (3), BD plates (4), unidirectional filter device (5), filter device (6) and solid-phase outlet (7) composition, the hollow rotating shaft (2) It is rotatably connected on the inside of the cone angle rotary drum (1), coaxially with hollow rotating shaft (2), the spiral transfers the cone angle rotary drum (1) Device (3) is fixed on the hollow rotating shaft (2), and the BD plates (4) are annular slab and are fixed on the hollow rotating shaft (2), institute It states BD plates (4) and the space between cone angle rotary drum (1) and hollow rotating shaft (2) is divided into left chamber body and right chamber body, the BD plates (4) There are spacing, the unidirectional filter device (5) to be arranged in the BD plates between outer end face and the inner surface of the cone angle rotary drum (1) (4) on, the filter device (6) and solid-phase outlet (7) are separately positioned on the both ends of the cone angle rotary drum (1), the filtering dress It sets (6) and is located at right chamber body end, the solid-phase outlet (7) is located at left chamber body end;
The cone angle rotary drum (1) is by cone section I (1-1), cone section II (1-2), cone section III (1-3), cone section IV (1-4) and cone section V (1-5) is formed, and the cone angle rotary drum (1) is respectively to bore section I (1-1), cone section II (1-2), III (1- of cone section from left end toward right end 3), cone section IV (1-4) and cone section V (1-5), the solid-phase outlet (7) are arranged on the cone section I (1-1), the filtering dress (6) are set to be arranged on the cone section V (1-5);
Feed inlet (2-1) and outlet (2-2), the feed inlet (2-1) and outlet (2-2) are provided on the hollow rotating shaft (2) Connection, the feed inlet (2-1) are located at one end of the hollow rotating shaft (2), and the outlet (2-2) is located at the cone angle rotary drum (1) inside and in right chamber body.
2. a kind of double tapered angle rotary drum according to claim 1, it is characterised in that:The cone section I (1-1) and cone section III (1-3) is parallel-segment, and the cone section II (1-2), cone section IV (1-4) and cone section V (1-5) are tilting section, the cone section II (1-2) is tilted outward, and the left end of the cone section II (1-2) is small end, and the right end of the cone section II (1-2) is big end, described Boring section IV (1-4) and cone section V (1-5), the angle of inclination of inclination and cone section V (1-5) is more than cone section IV (1-4) inwardly, described The left end for boring section IV (1-4) and cone section V (1-5) is big end, and the right end of the cone section IV (1-4) and cone section V (1-5) is small End.
3. a kind of double tapered angle rotary drum according to claim 1, it is characterised in that:The outer end face of the BD plates (4) and institute It is parallel to state cone section III (1-3), spacing between the two is 2-3mm, and cavity tilts the BD plates (4) to the left.
4. a kind of double tapered angle rotary drum according to claim 1, it is characterised in that:The unidirectional filter device (5) is more Hole ceramics so that only liquid can flow to right chamber body from left chamber body by unidirectional filter device (5).
5. a kind of double tapered angle rotary drum according to claim 1, it is characterised in that:The filter device (6) is porous pottery Porcelain, liquid for being discharged in right chamber body simultaneously prevent solid from being discharged.
6. a kind of double tapered angle rotary drum according to claim 1, it is characterised in that:The cone angle rotary drum (1) with hollow turn The junction of axis (2) is provided with sealing device.
CN201721904701.3U 2017-12-29 2017-12-29 A kind of double tapered angle rotary drum Active CN207970990U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721904701.3U CN207970990U (en) 2017-12-29 2017-12-29 A kind of double tapered angle rotary drum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721904701.3U CN207970990U (en) 2017-12-29 2017-12-29 A kind of double tapered angle rotary drum

Publications (1)

Publication Number Publication Date
CN207970990U true CN207970990U (en) 2018-10-16

Family

ID=63768486

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721904701.3U Active CN207970990U (en) 2017-12-29 2017-12-29 A kind of double tapered angle rotary drum

Country Status (1)

Country Link
CN (1) CN207970990U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108187925A (en) * 2017-12-29 2018-06-22 海申机电总厂(象山) A kind of double tapered angle rotary drum

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108187925A (en) * 2017-12-29 2018-06-22 海申机电总厂(象山) A kind of double tapered angle rotary drum

Similar Documents

Publication Publication Date Title
CN106824559B (en) Double-end reverse spiral material-pushing horizontal centrifuge
CN204294380U (en) A kind of double tapered angle drum structure of horizontal screw centrifuge
CN207970990U (en) A kind of double tapered angle rotary drum
JP2012187570A5 (en)
CN107755101B (en) Horizontal spiral sedimentation concentration centrifuge
CN108187925A (en) A kind of double tapered angle rotary drum
CN109453560A (en) Metal fillings recycles separator
CN205949084U (en) Centrifuge structure with two cone type spirochaetas
CN208516518U (en) A kind of production lithium battery precursor material Star-like unloader
CN207744703U (en) For the extraction element of papermaking-method reconstituted tobaccos and the system of production reconstituted tobacco
CN208612768U (en) A kind of centrifuge instrument of drilling mud purified treatment
CN210815749U (en) Horizontal spiral discharging sedimentation centrifuge with spiral circulating body
CN201260991Y (en) Decanter centrifuge
CN205274507U (en) Cement powder screw conveyor
CN205966199U (en) Flat swirler with adjustable center tube degree of depth
CN216654973U (en) Rotary drum for glufosinate-ammonium slurry dewatering centrifuge
CN209438824U (en) A kind of rotary drum being exclusively used in sludge Dewatering Centrifuge
CN208697733U (en) Dewaterer after a kind of cleaning of waste plastic
CN208824731U (en) A kind of raw mill powder concentrator
CN206838331U (en) A kind of Steviosin continuous centrifugal device
CN104668109A (en) Filtration aiding feeder on horizontal spiral discharge screen centrifuge
CN206981015U (en) A kind of horizontal centrifuge of big cone angle
CN212263584U (en) Double-cone centrifuge
CN201744408U (en) Disc separator dreg discharge device
CN209174357U (en) A kind of Chinese materia medica preparation processing raw material screening device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20201222

Granted publication date: 20181016

PD01 Discharge of preservation of patent
PD01 Discharge of preservation of patent

Date of cancellation: 20231222

Granted publication date: 20181016

PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20240314

Granted publication date: 20181016