CN105381740A - Energy adaptation-based grading surface modification paste mixer - Google Patents
Energy adaptation-based grading surface modification paste mixer Download PDFInfo
- Publication number
- CN105381740A CN105381740A CN201510941314.6A CN201510941314A CN105381740A CN 105381740 A CN105381740 A CN 105381740A CN 201510941314 A CN201510941314 A CN 201510941314A CN 105381740 A CN105381740 A CN 105381740A
- Authority
- CN
- China
- Prior art keywords
- mixing
- room
- paste
- size mixing
- ore pulp
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/85—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts
- B01F27/851—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts the receptacle being subdivided in adjacent compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/70—Pre-treatment of the materials to be mixed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/86—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/87—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the receptacle being divided into superimposed compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71725—Feed mechanisms characterised by the means for feeding the components to the mixer using centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/50—Mixing mined ingredients and liquid to obtain slurries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention discloses an energy adaptation-based grading surface modification paste mixer. The paste mixer comprises a paste mixing barrel. The paste mixing barrel is divided into an upper paste mixing chamber and a lower paste mixing chamber and the two chambers are separated by a separation plate. A hydrocyclone grading part is fixed to the middle of the separation plate. An overflow port of the hydrocyclone grading part is communicated with the upper paste mixing chamber. A bottom port is communicated with the lower paste mixing chamber. Each one of the upper and lower paste mixing chambers is provided with a stirrer, a motor, a stirring baffle plate, a feeding pipe port and a paste outlet. Through combination of the stirrers, the motors, the stirring baffle plates, the feeding pipe ports and the upper and lower paste mixing chambers, coarse and fine materials are reasonably matched according to requirements on energy input and agent use amounts so that the coarse and fine materials are subjected to blending pre-treatment. The paste mixer is an ore paste pre-treatment device with a simple structure, economy and high efficiency.
Description
Technical field
The present invention relates to a kind of coal slime flotation size mixing equipment, particularly relate to a kind of stepped surface upgrading paste mixer based on energy adaptation.
Background technology
Coal is the basic energy resource of world's important energy source, Ye Shi China.While coal supports China's rapid economic development, as non-renewable resources, the reserves of coal constantly reduce, and the high-efficiency cleaning of coal resources utilizes significant.Along with the raising of mining mechanization degree, the coal amount in feed coal is along with increase, and efficient separation and the crucial focus be recycled in order to enterprise's upgrading synergy of Bed for Fine Coal are also the important embodiments of coal resources efficiency utilization simultaneously.Flotation technology is as the most effective fine coal slime separation method, and flotation operation becomes more and more important.And size mixing as the first step operation of flotation operation, will directly affect the separation index of flotation.
An important function of sizing mixing enables collecting agent be adsorbed onto object ore particle surface exactly, improves mineral floatability and flotation speed.But in the process of sizing mixing, fine beans is because its granularity is little, specific area is large, competitive Adsorption can be formed with Coarse Coal, thus cause adsorbing in floatation process, with occurring fine beans poor selectivity a large amount of medicament and low grey Coarse Coal is not adsorbed onto collecting agent and is lost in tail coal.There is this problem, different closely related with the energy requirement of sizing mixing of fine beans and Coarse Coal.
Existing size mixing equipment is all the equipment of the homogeneous input of energy.Energy input is high, and the paste mixer that shear strength is large can improve microfine coal yield, but result also in the loss of Coarse Coal simultaneously, and floatation clean coal productive rate declines; Energy input is low, and the size mixing equipment that shear strength is little can ensure the recovery of Coarse Coal, but the weak effect of sizing mixing to fine beans, causes that floatation clean coal ash content is high, productive rate is low.For this problem, develop a kind of stepped surface upgrading size mixing equipment based on energy adaptation, the difference of adaptive thickness beans is sized mixing energy requirement, and improve effect of sizing mixing, the efficiency utilization of intensified Daqu to the efficient separation and coal resources that realize Bed for Fine Coal is very meaningful.
Summary of the invention
The object of the present invention is to provide a kind of stepped surface upgrading paste mixer based on energy adaptation, the difference of adaptive thickness beans is sized mixing energy requirement, improves effect of sizing mixing, intensified Daqu operation.
The present invention is achieved through the following technical solutions:
A kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention, comprises mixing cirtern, and mixing cirtern divides two sections to size mixing room, and two rooms of sizing mixing are separated by dividing plate, and mixing cirtern center is provided with cyclone classification parts, and is fixed by dividing plate.Described mixing cirtern is sized mixing bottom, room is provided with stock inlet, and stock inlet is connected with cyclone classification parts; Upper and lower two rooms of sizing mixing are provided with independent agitating device, and are provided with grout outlet on the top of two rooms of sizing mixing respectively, and bottom is provided with blowing mouth; And be provided with the independent dosing mouth of pipe in upper and lower two sides of sizing mixing room.
As can be seen from the technical scheme of the invention described above, a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention is owing to being provided with cyclone classification parts in mixing cirtern, ore pulp is after stock inlet enters mixing cirtern, through cyclone classification part classification, the shunting of ore pulp based on granularity thickness can be realized; A kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention to be sized mixing room be furnished with independent agitating device and dosing mouth owing to being provided with upper and lower two, fine ore pulp ore pulp after classified by the top discharge mouth of cyclone classification parts enter mixing cirtern on to size mixing room, coarse-grained material ore pulp is sized mixing under entering mixing cirtern by the lower discharge port of cyclone classification parts room.On the agitating device of the room of sizing mixing configuration, energy input is high, and shear strength is large, is applicable to fine beans and sizes mixing; Under the room of sizing mixing configuration agitating device, energy input low, shear strength is little, and applicable Coarse Coal is sized mixing; After classification is sized mixing, size mixing from above room grout outlet of microfine ore pulp is discharged, and coarse grain ore pulp room grout outlet of sizing mixing by is down discharged.
A kind of advantage had based on the stepped surface upgrading paste mixer of energy adaptation of the present invention is, can adaptive thickness material for size mixing energy input demand non-equilibrium, the difference meeting thickness material ore pulp is sized mixing demand, entirety improves effect of sizing mixing, achieve the effective absorption of fine-particle minerals to the selective absorption of floating agent and Coarse Coal Mineral pairs floating agent, to solve in follow-up flotation operation the thin mud of the high ash of microfine and pollute cleaned coal due to poor selectivity and low grey Coarse Coal causes being lost in floating tail-coal owing to effectively not adsorbing collecting agent the problem causing clean coal yield to reduce, enhance flotation.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of patent of the present invention, below the accompanying drawing used required in describing embodiment is briefly described.Apparently, the accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, can also obtain other accompanying drawings according to these accompanying drawings.
Fig. 1 is the structural representation of a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention.
In Fig. 1: 1-stock inlet; 2-cyclone classification parts; 3-to size mixing room agitating device; To size mixing under 4-room agitating device; 5-to size mixing room grout outlet; To size mixing under 6-room grout outlet; 7-to size mixing room blowing mouth; To size mixing under 8-room blowing mouth; 9-to size mixing the room dosing mouth of pipe; To size mixing under 10-the room dosing mouth of pipe; 11-mixing baffle; 12,13-motor; 14-to size mixing room; To size mixing under 15-room.
Fig. 2 is a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention for the schematic diagram of bulk flotation technique after sizing mixing.
Fig. 3 is a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention for the schematic diagram of stage flotation technique after sizing mixing.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in one embodiment of the present of invention is clearly and completely described.Obviously, described embodiment is only the present invention's part embodiment, instead of whole embodiments.Based on embodiments of the invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to protection scope of the present invention.
A kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention, preferably detailed description of the invention is as shown in Figure 1 for it, mixing cirtern comprise size mixing room 14 and under to size mixing room 15, two rooms of sizing mixing are separated by dividing plate, on size mixing in room 14 and be axially arranged with agitating device 3, driven by motor 12, under size mixing to be axially arranged with in room 15 and be inverted and the agitating device 4 of sealing, driven by motor 13, also can adopt other set-up mode.
To size mixing demand according to the difference of thickness material ore pulp, on to size mixing impeller agitating device 3 preferentially selected in room 14 and easily produce high shear force shape, also can multilayer arrange, and under to size mixing impeller agitating device 4 preferentially selected in room 15 and not easily produce high shear force shape.
On the size mixing bottom of room 14 be provided with stock inlet 1, stock inlet 1 is connected with cyclone classification parts 2, cyclone classification parts 2 are fixed by dividing plate, ore pulp is after stock inlet 1 enters cyclone classification parts 2, ore pulp material is classified to fine ore pulp and coarse-grained material ore pulp, by the overfall of cyclone classification parts 2 and underflow opening enter respectively size mixing room 14 and under to size mixing room 15.On size mixing room 14 and under the size mixing side of room 15 be configured with the dosing mouth of pipe 9 and 10 respectively, the sidewall of two rooms of sizing mixing is arranged mixing baffle 11, according to different needs, the width of upper and lower mixing baffle can be different.
After the classification of thickness material ore pulp is sized mixing, fine ore pulp room grout outlet 5 of sizing mixing from is above discharged, coarse-grained material ore pulp room grout outlet 6 of sizing mixing by is down discharged, after discharging, both go flotation after can collaborating mixing, as shown in Figure 2, also the floatation equipment of applicable respective grade can be gone separately to carry out flotation, as shown in Figure 3.
Operation principle and the course of work: ore pulp is fed with the stock inlet of certain pressure from a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention by pump, and tangent line feeds cyclone classification parts obtains a point level shunt, its overflow (fine ore pulp) enters into room of sizing mixing, and underflow (coarse-grained material ore pulp) enters into down room of sizing mixing.On the size mixing agitating device of room be furnished with the impeller easily producing high shear force shape, in conjunction with the high-energy input of motor and the acting in conjunction of mixing baffle, make particulate target minreal and medicament carry out selectively adsorbing.Under the size mixing agitating device of room be furnished with the impeller not easily producing high shear force shape, the energy input suitable in conjunction with motor and the acting in conjunction of mixing baffle, enable coarse grain target minreal and medicament carry out fully and effectively adsorbing, make large or fine granule can obtain the floating product of high-quality.Material ore pulp after sizing mixing enters into follow-up floatation equipment through grout outlet discharge and carries out flotation, obtains floatation clean coal and floating tail-coal.
A kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention, in energy input and dosing is adaptive reasonable, economy higher while, meet thickness material to the different demands of sizing mixing on environment and floating agent dosage, thickness material can be sized mixing pretreating effect preferably, is that a kind of structure is simple, the ore pulp pretreatment unit of economical and efficient.
The above; be only the present invention's preferably detailed description of the invention, but protection scope of the present invention is not limited thereto, is anyly familiar with those skilled in the art in the technical scope that the present invention discloses; the change that can expect easily or replacement, all should be encompassed within protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with the protection domain of patent claim.
Claims (4)
1. a kind of stepped surface upgrading paste mixer based on energy adaptation of the present invention, it is characterized in that: it comprises mixing cirtern, mixing cirtern comprise size mixing room and under to size mixing room, two rooms of sizing mixing are separated by dividing plate, on indoor of sizing mixing be axially arranged with agitating device, driven by motor, under indoor of sizing mixing be axially arranged with and be inverted and the agitating device of sealing, driven by motor, also can adopt other set-up mode.
2. a kind of stepped surface upgrading paste mixer based on energy adaptation according to claim 1, it is characterized in that: to size mixing demand according to the difference of thickness material ore pulp, on to size mixing impeller agitating device preferentially selected in room and easily produce high shear force shape, also can multilayer arrange, and under to size mixing impeller agitating device preferentially selected in room and not easily produce high shear force shape.
3. a kind of stepped surface upgrading paste mixer based on energy adaptation according to claim 2, it is characterized in that: the bottom of room of above sizing mixing is provided with stock inlet, stock inlet is connected with cyclone classification parts, cyclone classification parts are fixed by dividing plate, ore pulp is after stock inlet enters cyclone classification parts, ore pulp material is classified to fine ore pulp and coarse-grained material ore pulp, by the overfall of cyclone classification parts and underflow opening enter respectively size mixing room and under to size mixing room.
4. a kind of stepped surface upgrading paste mixer based on energy adaptation according to claim 3, it is characterized in that: above size mixing room and under size mixing the side of room be configured with respectively the dosing mouth of pipe and, the sidewall of two rooms of sizing mixing arranges mixing baffle, according to different needs, the width of upper and lower mixing baffle can be different.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510941314.6A CN105381740A (en) | 2015-12-16 | 2015-12-16 | Energy adaptation-based grading surface modification paste mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510941314.6A CN105381740A (en) | 2015-12-16 | 2015-12-16 | Energy adaptation-based grading surface modification paste mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105381740A true CN105381740A (en) | 2016-03-09 |
Family
ID=55414893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510941314.6A Pending CN105381740A (en) | 2015-12-16 | 2015-12-16 | Energy adaptation-based grading surface modification paste mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105381740A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1597129A (en) * | 2004-09-02 | 2005-03-23 | 曾兴民 | Hydraulic conical drum sieve |
| CN1603002A (en) * | 2004-10-29 | 2005-04-06 | 东北大学 | Highly efficient ore dressing system of medium-low class aluminium ore |
| US20080025143A1 (en) * | 2004-09-15 | 2008-01-31 | Hiroaki Ohashi | Apparatus and Method for Solid-Liquid Contact |
| CN101543739A (en) * | 2009-03-27 | 2009-09-30 | 中国矿业大学(北京) | Surface modification pulp mixing machine and application thereof |
-
2015
- 2015-12-16 CN CN201510941314.6A patent/CN105381740A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1597129A (en) * | 2004-09-02 | 2005-03-23 | 曾兴民 | Hydraulic conical drum sieve |
| US20080025143A1 (en) * | 2004-09-15 | 2008-01-31 | Hiroaki Ohashi | Apparatus and Method for Solid-Liquid Contact |
| CN1603002A (en) * | 2004-10-29 | 2005-04-06 | 东北大学 | Highly efficient ore dressing system of medium-low class aluminium ore |
| CN101543739A (en) * | 2009-03-27 | 2009-09-30 | 中国矿业大学(北京) | Surface modification pulp mixing machine and application thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11358152B2 (en) | Underground coal separation process adopting water medium | |
| CN102430481B (en) | Sorting process for high-ash and difficult-separation coal slime | |
| CN104722389B (en) | Coal dissociation-is independently sized mixing-bulk flotation technique in a kind of particulate | |
| WO2020181618A1 (en) | Underground coal preparation process | |
| CN105170306B (en) | A kind of washing process for the high high high spoil coal of mud of ash | |
| CN203525901U (en) | Slurry treatment device for slurry shield construction | |
| CN104826727B (en) | Coal Multistage ore-grinding floatation process and system in a kind of particulate | |
| CN110201790B (en) | Sorting and recycling system and sorting and recycling process for wide-size coal slime | |
| CN106179717A (en) | A kind of full level of thermal coal is selected in simplified heavy medium sorting process | |
| CN104815748B (en) | The broken mill floatation process of two sections of coal in a kind of coking | |
| CN202129156U (en) | Three-product autogenous medium cyclone for coarse coal slime separation | |
| CN103752414A (en) | Pulp mixing reinforced deep flotation technology process | |
| CN203635312U (en) | Mineral tailings grading and separating recovery system for middings magnetic separator in dense medium coal preparation plant | |
| CN110385197B (en) | Gravity separation system and process for barite fluorite associated ore | |
| CN204672415U (en) | Ilmenite combined classification separation system | |
| CN104437828A (en) | Efficient desulfuration and deashing dense medium separation technology for fine coal | |
| CN105964392A (en) | Coal dressing and desliming system | |
| CN107008564B (en) | The method of the dense media rate of recovery is improved in a kind of coal preparation technique | |
| CN104437832A (en) | Dry-method fines removal dense medium sorting process for slack coal flip-flow screen | |
| CN203862375U (en) | Washing and selecting device targeted for high-ash high-mud high-gangue coal | |
| CN103785529B (en) | A kind of washing appliance for high grey high mud height spoil coal | |
| CN105381740A (en) | Energy adaptation-based grading surface modification paste mixer | |
| CN205412751U (en) | Hierarchical surface -changing paste mixer based on energy adaptation | |
| CN110302894B (en) | Desilication method for producing bauxite concentrate by using ultra-low grade raw ore | |
| CN209271642U (en) | Tertiary industry product liquid-solid fluid bed separation coarse slime system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160309 |