CN202762553U - Plate -type coal ash multistage flotation separation equipment - Google Patents

Plate -type coal ash multistage flotation separation equipment Download PDF

Info

Publication number
CN202762553U
CN202762553U CN 201220360925 CN201220360925U CN202762553U CN 202762553 U CN202762553 U CN 202762553U CN 201220360925 CN201220360925 CN 201220360925 CN 201220360925 U CN201220360925 U CN 201220360925U CN 202762553 U CN202762553 U CN 202762553U
Authority
CN
China
Prior art keywords
flotation
separation equipment
gas diffusion
ash
flotation separation
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.)
Expired - Fee Related
Application number
CN 201220360925
Other languages
Chinese (zh)
Inventor
许闽清
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.)
FUJIAN LONGYAN LONGNENG FLY ASH COMPREHENSIVE UTILIZATION Co Ltd
Original Assignee
FUJIAN LONGYAN LONGNENG FLY ASH COMPREHENSIVE UTILIZATION 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 FUJIAN LONGYAN LONGNENG FLY ASH COMPREHENSIVE UTILIZATION Co Ltd filed Critical FUJIAN LONGYAN LONGNENG FLY ASH COMPREHENSIVE UTILIZATION Co Ltd
Priority to CN 201220360925 priority Critical patent/CN202762553U/en
Application granted granted Critical
Publication of CN202762553U publication Critical patent/CN202762553U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

The utility model provides a plate -type coal ash multistage flotation separation equipment. The plate -type coal ash multistage flotation separation equipment comprises a groove body in elongated shape. The groove body is composed of a head portion and an end portion, wherein the upper portion of the head portion or the top of the head portion is provided with a raw material inlet, and a flotation outlet is arranged on the upper portion of the end portion or the top. The groove is divided into at least two flotation units by at least a plate device. The bottom of each flotation unit is evenly provided with a tail ash outlet. The multistage flotation separation equipment further comprises an aerating apparatus used for producing air bubbles, wherein the aerating apparatus comprises air bubble diffusing devices which are respectively located inside each flotation unit, and the amount of the air bubble diffusing devices is equal to the amount of the flotation units. Each air bubble diffusing device evenly comprises a gas diffusion hole used for the overflow of an air bubble, and a gas diffusion tube. Each plate device evenly comprises an adjusting weir flow board. The size of an overflow hole on the plate device can be adjusted through the depth adjustment or the height adjustment of the weir flow board. The multistage flotation separation equipment has the advantages of being little in power consumption, simple in structure, easy to process and capable of reducing production costs. Meanwhile, the ash content of high charcoal ash obtained from the utilization of the device flotation can be reduced by a range from about three percent to five percent, thereby improving flotation effect and obtaining the high charcoal ash with high carbon content.

Description

Board plug type ash multilevel flotation separation equipment
Technical field
The utility model relates to and utilizes flyash to make active carbon, and more particularly, the utility model relates to a kind of board plug type ash multilevel flotation separation equipment.
Background technology
The main component of flyash is ash content and the unburned charcoal particle that comprises the oxides such as silica, alundum (Al2O3), di-iron trioxide, calcium oxide, magnesia, sulfur trioxide, and wherein unburned charcoal particle can be used as the raw material of producing active carbon after extracting.
Because the charcoal particle is lighter, usually use the charcoal particle in the mode extract powder coal ash of flotation.Prior art provide multiple from flyash the equipment of flotation carbon particle.For example, Chinese patent 200810031474.7 discloses a kind of flotation pillar special for fly ash, at flotation column cylindrical shell top pulp distributer is housed, establish multilayer bubbling plate in the cylindrical shell, multiple spot swirl-flow devices and multiple spot tail ash spout hole are established in the cylindrical shell bottom, install the ore pulp distributing pipe around the pulp distributer, around device circulating line, the circulating line upper end connects with the ore pulp distributing pipe, lower end and swirl-flow devices connect, ore pulp distributing pipe interface and feed inlet and outlet respectively connect the circulating pump two ends, the high charcoal balanced overflow plate of ash and the overflow of high charcoal ash also are housed on flotation column top collect mouthful, and tail ash spout hole is connected and installed with tail ash automatic control stuff box by pipeline.
And for example, Chinese patent 200920064391.8 discloses a kind of floatation column special for circulating fluidized, at the top pulp distributer is housed, in establish multilayer bubbling plate, the multiple spot swirl-flow devices is established in the bottom, the bottom is connected and installed taper tail ash feeder, install the ore pulp distributing pipe around the pulp distributer, the peripheral device circulating line, the ore pulp distributing pipe connects circulating pump, the high charcoal balanced overflow plate of ash also is housed on flotation column top and collects mouth, the tail ash tube road that its bottom of taper tail ash feeder connects is connected to tail ash automatic control stuff box.
And for example, Chinese patent 200820046239.2 discloses a kind of flyash flotation carbon process units, flyash flotation carbon process units comprises the screening module that can screen the flyash granularity, stirs module, can cleaned coal and tail ash content from flotation module, dehydration module and the conveying mechanism that becomes integral body with upper module successively organic connections.
The said equipment all is the device that flyash is carried out the one-level flotation, in the production practices, in order to obtain the higher high charcoal ash of phosphorus content with the higher active carbon of preparation quality, can carry out again flotation to the particle that the one-level flotation obtains.For example, Chinese patent 200920063583.7 discloses a kind of new equipment of producing active carbon with flyash, comprises that the former ash of flyash that connects successively advances ash bucket, electronic measuring scale, box-type ash remover, ore pulp preprocessor, first order flotation column, second level flotation column, the first thickener, the first filter, the first dryer, active carbon Special grinding, oil water separator, the second dryer; Ore pulp preprocessor and second level flotation column also are connected with the automatic medicament feeding machine of dispersant and composite floating chemical, and the active carbon Special grinding also is connected with the high steam pipeline.This equipment carries out secondary floatation by first order flotation column and second level flotation column are set to flyash, because the structure of every one-level flotation column more complicated all, the structure of this secondary floatation system is more complicated, and then causes its material cost and processing cost high; Because power consumption is large, its operating cost is higher simultaneously; In addition, its flotation effect is unsatisfactory.
Summary of the invention
For the shortcoming of prior art, the purpose of this utility model provides the multistage flotation separation equipment that a kind of interposed structure is simple, cheap for manufacturing cost, power consumption is little and flotation effect is good.
To achieve these goals, the utility model provides a kind of board plug type ash multilevel flotation separation equipment, and it comprises the groove shape body of strip, and this groove shape body comprises stem and afterbody, wherein the top of stem or top are provided with the feed(raw material)inlet, and the top of afterbody or top are provided with the flotation outlet; This groove shape body is separated at least two flotation cells by at least one board plug device; The bottom of each flotation cells is equipped with the outlet of tail ash; This multistage flotation separation equipment also comprises the aerator for generation of bubble, aerator comprises consistent with the flotation cells number and lays respectively at bubble diffusing apparatus in each flotation cells, and each bubble diffusing apparatus includes gas diffusion hole or the gas diffusion tube of overflowing for bubble; Each board plug device includes adjusting weir flow plate movable up and down, by the depth adjustment of regulating the weir flow plate or the size of highly regulating this board plug device overflow discharge orifice.
In the utility model, in order to reach preferably flotation effect, usually the spout hole on the board plug device is located at top.By regulating the adjusting weir flow plate of board plug device, regulate the size of the spout hole of the board plug device between the adjacent flotation cells, and then regulate the degree that fluid is communicated with between the adjacent flotation cells.For example, regulate the weir flow plate and can regulate from the top of equipment, also can regulate from the bottom of equipment.
In the utility model, the number of board plug device is more, and the quantity of the flotation cells that separates is more, the effect of flotation is better, but reach some when flotation cells, increase again the flotation effect that one section flotation cells improves more small, just there is no need to increase flotation cells this moment.Weigh the flotation effect of expection and make operating cost, preferred flotation cells number is two, three or four.
In the utility model, aerator is to produce bubble for the working solution in liquid or liquid-solid mixing.It both can be various blast aerators, for example (little) stingy alveolitoid, middle air bubble type, atmosphere alveolitoid, hydraulic shear type, hydraulic blow type blast aerator; Can be again various Mechanical aerators, such as pump type impeller aerator, K type impeller aerator, inversed umbrella type impeller aerator and plate impeller aerator etc.; Also can be the aerator of other type.It is preferably blast aerator commonly used in the sewage disposal, hydraulic shear type air-diffuser for example, but the construction features of its use device itself, produce the hydraulic shear effect, air pocket is cut into minute bubbles, increase the gas-liquid contact area, reach the purpose of raising the efficiency, as decide spiral aerator etc.
In the utility model, bubble diffusing apparatus can be the concentric tube that interconnects between tabular, bend pipe, parallel pipe, coil pipe or the adjacent channel of hollow, which is provided with a plurality of gas diffusion hole or gas diffusion tube of overflowing for bubble; Also can be a plurality of above-mentioned platy structures or tubular structure be arranged in parallel up and down.
In the utility model, when bubble diffusing apparatus overflows bubble by gas diffusion tube, but these a plurality of body anemostat directions straight up as one man, also can be set to separately with different angle points upwards or oblique upper, so that the material in the flotation cells forms turbulent flow.By making the gas that upwards blows be turbulent condition, the time of contact of carbon granule and bubble is long, contacts more fully, and the probability that fly ash grain is broken for carbon granule and ash particles increases greatly, thereby so that flotation effect is better, flotation efficiency is higher.
Operation principle of the present utility model is: the main component of flyash is carbon granule and ash content.After adding flotation agent and/or collecting agent and/or other auxiliary agent, the particle in the flyash contacts, collides with bubble, and the carbon granule that floatability is good optionally adheres to bubble, and is carried rising, realizes flotation.The poor ash content of floatability is then to sinking.
Workflow of the present utility model is: the mixture of powdered coal ash and flotation agent enters in the first section flotation cells.The exhaust in the first section flotation cells of the aeration head of aerator, carbon granule adhere to bubble and scatter floating and move upward under the effect of flotation agent, the hole of the carbon granule that floatingly selects on board plug device enters next section flotation cells.Carbon granule in this section flotation cells, repeat with first section flotation cells in the same process, carry out entering next section flotation cells after the again flotation ... by that analogy, obtain the high charcoal ash that obtains through multistage flotation from the flotation outlet of rear flotation cells at last.
In the Multi-stage flotation equipment of the present utility model, power consumption unit only is aerator, and its power consumption is very little, thereby has greatly saved the energy; Aerator and board plug device all can be outsourcing piece, simultaneously flotation plate, mortar pump are not set, make Multi-stage flotation equipment of the present utility model simple in structure, are easy to processing, and have reduced manufacturing cost; In addition, utilize Multi-stage flotation equipment of the present utility model, the ash content in the high charcoal ash that flotation obtains can fall about 3%-5%, has improved flotation effect, obtains the higher high charcoal ash of phosphorus content.
According to the utility model one specific embodiment, aerator is blast aerator, and it comprises that wind send device, gas transmission pipeline, bubble diffusing apparatus, and this wind send device to link to each other with each bubble diffusing apparatus by gas transmission pipeline.According to another specific embodiment of the utility model, the gas diffusion hole of each bubble diffusing apparatus or the number of gas diffusion tube are 3-15, and are divided into multilayer and arrange.
According to another specific embodiment of the utility model, each bubble diffusing apparatus comprises 8 gas diffusion holes or gas diffusion tube, these 8 gas diffusion holes or gas diffusion tube are divided staggered two-layer up and down, 4 every layer, the angle between adjacent two gas diffusion holes of same layer or the gas diffusion tube is 90 °.
According to another specific embodiment of the utility model, it is air-blast device or air compression plant that wind send device.For example, a capacity is 6m 3/ min, pressure are that 0.7MPa, power are the air compressor of 37KW, can be for three aerators simultaneously.
According to the utility model one specific embodiment, each board plug device also comprises fixing insertion.Fixing insertion and adjusting weir flow plate are realized the plate function jointly.Particularly, for example, can make fixing insertion be positioned at the bottom, regulate the weir flow plate and be positioned at top.Space between the bottom of adjusting weir flow plate and the top of fixing insertion is the spout hole of this board plug device.
According to another specific embodiment of the utility model, each flotation cells includes superposed cylindrical shell and is positioned at the tail ash gathering-device of bottom; Board plug device consists of the part of cylindrical shell barrel; Tail ash gathering-device is that the cone of pointed end is bucket-shaped, and the outlet of tail ash is positioned at the place, tip of tail ash gathering-device bottom.
According to another specific embodiment of the utility model, in each flotation cells, the intersection of cylindrical shell and tail ash gathering-device is provided with filter, to slow down the downstream rate of material.According to another specific embodiment of the utility model, each filter all is obliquely installed, and each filter is positioned at same inclined-plane; The height of a plurality of bubble diffusing apparatus reduces to rear successively from first section.According to another specific embodiment of the utility model, each filter all is horizontally disposed with, and each filter is positioned at same plane; Each bubble diffusing apparatus height is consistent.Certainly, also filter can be set, but the intersection of the cylindrical shell of all flotation cells and tail ash gathering-device is positioned at same plane or same inclined-plane.
According to another specific embodiment of the utility model, flotation separation equipment also comprises feed preparing device, the bottom of feed preparing device or bottom connect charging line, charging line leads to the feed(raw material)inlet, the flyash for the treatment of flotation adds the chemical agents such as flotation agent in feed preparing device, then the charging line of the bottom through being positioned at feed preparing device or bottom enters first section flotation cells.According to another specific embodiment of the utility model, can be provided with agitating device in the feed preparing device, be used for powdered coal ash slurry and flotation agent are fully stirred.Charging line is provided with feeding engine, is used for the material pumping in the feed preparing device in first section flotation cells.
According to another specific embodiment of the utility model, the outlet of tail ash connects the tail ash tube road, and the tail ash tube road is controlled it by valve and led to feed preparing device or tail ashpit.Operating personnel judge by the phosphorus content in the tail ash, if the phosphorus content in the tail ash is higher, then controls this tail ash by valve and lead to feed preparing device, reenter the feed(raw material)inlet of first section flotation cells in feed preparing device behind the adding flotation agent, carry out again flotation; If the phosphorus content in the tail ash is lower, then controls this tail ash by valve and lead to the tail ashpit.
According to another specific embodiment of the present utility model, flotation separation equipment also can comprise the barrel that is positioned at flotation separation equipment or the physical separation means on the bubble diffusing apparatus.By physical separation means is set, effectively break the combination between carbon granule and the ash content, greatly improved the flotation rate of carbon.This physical separation means specifically can be ultrasonic separation means or ultrasonic broken in bulk putting, and improves peeling off of carbon granule and ash content by the emission ultrasonic wave, for example, forms granularity and reaches the ultra-fine carbon granule of 10,000 purposes.Particularly, this ultrasonic separation means or ultrasonic broken in bulk putting comprise ultrasonic transmitter and supporting servicing unit.
Compared with prior art, the utlity model has following beneficial effect:
In the Multi-stage flotation equipment of the present utility model, power consumption unit only is aerator, and its power consumption is very little, thereby has greatly saved the energy; Aerator and board plug device all can be outsourcing piece, simultaneously flotation plate, mortar pump are not set, make Multi-stage flotation equipment of the present utility model simple in structure, are easy to processing, and have reduced manufacturing cost; In addition, utilize Multi-stage flotation equipment of the present utility model, the ash content in the high charcoal ash that flotation obtains can fall about 3%-5%, has improved flotation effect, obtains the higher high charcoal ash of phosphorus content.
The utility model is described in further detail below in conjunction with accompanying drawing.
Description of drawings
Fig. 1 is that embodiment 1 of the present utility model is along the structural representation of the longitudinal section of its axis;
Fig. 2 is that embodiment 2 of the present utility model is along the structural representation of the longitudinal section of its axis.
The specific embodiment
Embodiment 1
As shown in Figure 1, the slot type flotation separation equipment of the present embodiment comprises: the groove shape body of feed preparing device 11, strip, for generation of the aerator (for example blast aerator) of bubble.
The bottom of feed preparing device 11 connects charging line 1102, and charging line logical 1102 is provided with agitating device 1101 to the feed(raw material)inlet in the feed preparing device 11, and charging line 1102 is provided with feeding engine 1103.
The groove shape body of strip comprises stem and afterbody, and the top of described stem is provided with the feed(raw material)inlet, and the top of afterbody is provided with the flotation outlet; This groove shape body is separated into four flotation cells by three board plug devices, respectively headed by section flotation cells 12, second segment flotation cells 13, the 3rd section flotation cells 14, rear flotation cells 15.
Board plug device between first section flotation cells 12 and the second segment flotation cells 13 comprises fixing insertion 1202 and adjusting weir flow plate 1203 movable up and down, and fixing insertion 1202 is positioned at the bottom, regulates weir flow plate 1203 and is positioned at top.Space between the bottom of adjusting weir flow plate 1203 and the top of fixing insertion 1202 is the spout hole of this board plug device.
The top of first section flotation cells 12 is provided with the feed(raw material)inlet, the tail ash gathering-device 1204 that it is included in the cylindrical shell on top and is positioned at the bottom, and the intersection of cylindrical shell and tail ash gathering-device 1204 is provided with filter.Tail ash gathering-device 1204 is that the cone of pointed end is bucket-shaped, and the place, tip of tail ash gathering-device 1204 bottoms is provided with the outlet of tail ash.The outlet of tail ash connects tail ash tube road 1205, and the other end in tail ash tube road 205 is connected to tail ash total pipeline 17.Tail ash total pipeline 17 leads to feed preparing device 11 or tail ashpit by valve 1801 and valve 1802 controls.
Blast aerator comprises that wind send device (for example air compressor 16), gas transmission pipeline 1603, lays respectively at four bubble diffusing apparatus in each flotation cells, air compressor 16 links to each other with each bubble diffusing apparatus by gas transmission pipeline 1603, and this gas transmission pipeline 1603 is provided with valve 1601 and flowmeter 1602.
The bubble diffusing apparatus 1201 that is positioned at first section flotation cells 12 comprises 8 gas diffusion tube, and these 8 gas diffusion tube are divided staggered two-layer up and down, and 4 every layer, the angle between adjacent two gas diffusion tube of same layer is 90 °.These 8 gas diffusion tube are set to separately with different angle points upwards or oblique upper.
Structure and the bubble diffusing apparatus thereof of second segment flotation cells 13, the 3rd section flotation cells 14, rear flotation cells 15 are all similar with first section flotation cells 12.The top of rear flotation cells 15 is provided with the flotation outlet.
Each filter all is horizontally disposed with, and each filter is positioned at same plane; The height of each bubble diffusing apparatus is consistent.
The capacity of air compressor 16 is 8m 3/ min, power are 50KW, can be for four bubble diffusing apparatus simultaneously.
In the present embodiment, the power consumption unit that the mixed material in the floatation equipment is moved upward is air compressor (50KW/ platform), and namely to make mixed material in the floatation equipment institute's wasted work rate that moves upward be 50KW to the present embodiment.In order to reach identical effect, use the level Four flotation separation equipment institute wasted work rate of Venturi tube to be every grade of 55KW of 220KW().
About the content of ashes 3%-4% in the high charcoal ash that the flotation by the present embodiment obtains, and the content of ashes in the high charcoal ash that the flotation separation equipment flotation of prior art obtains is about 20%.
Embodiment 2
As shown in Figure 2, embodiment 2 of the present utility model is with the difference of embodiment 1:
1, is divided into three sections flotation cells by two board plug devices, section flotation cells 22, second segment flotation cells 23, rear flotation cells 24 headed by distinguishing;
2, each filter all is obliquely installed, and each filter is positioned at same inclined-plane;
3, the height of a plurality of bubble diffusing apparatus reduces to rear successively from first section;
4, the capacity of air compressor is 6m 3/ min, pressure are that 0.7MPa, power are 37KW, can be for three bubble diffusing apparatus simultaneously.
In the present embodiment, the power consumption unit that the mixed material in the floatation equipment is moved upward is air compressor (37KW/ platform), and namely to make mixed material in the floatation equipment institute's wasted work rate that moves upward be 37KW to the present embodiment.In order to reach identical effect, use three grades of flotation separation equipment institute wasted work rates of Venturi tube to be every grade of 55KW of 165KW().
About the content of ashes 3%-5% in the high charcoal ash that the flotation by the present embodiment obtains, and the content of ashes in the high charcoal ash that the flotation separation equipment flotation of prior art obtains is about 20%.
Although the utility model discloses as above with preferred embodiment, be not to limit the scope that the utility model is implemented.Any those of ordinary skill in the art, within not breaking away from invention scope of the present utility model, when doing a little improvement, namely every equal improvement of doing according to the utility model should be invention scope of the present utility model and contains.

Claims (10)

1. a board plug type ash multilevel flotation separation equipment is characterized in that, comprises the groove shape body of strip, and described groove shape body comprises stem and afterbody, and top or the top of described stem are provided with the feed(raw material)inlet, and the top of described afterbody or top are provided with the flotation outlet; Described groove shape body is separated at least two flotation cells by at least one board plug device; The bottom of each described flotation cells is equipped with the outlet of tail ash; Described multistage flotation separation equipment also comprises the aerator for generation of bubble, described aerator comprises consistent with described flotation cells number and lays respectively at bubble diffusing apparatus in each flotation cells, and each described bubble diffusing apparatus includes gas diffusion hole or the gas diffusion tube of overflowing for bubble; Each described board plug device includes adjusting weir flow plate movable up and down, by the depth adjustment of regulating the weir flow plate or the size of highly regulating this board plug device overflow discharge orifice.
2. multistage flotation separation equipment as claimed in claim 1, it is characterized in that, described aerator is blast aerator, and it comprises that wind send device, gas transmission pipeline, bubble diffusing apparatus, and described wind send device to link to each other by the described bubble diffusing apparatus of gas transmission pipeline and each.
3. multistage flotation separation equipment as claimed in claim 2 is characterized in that, the gas diffusion hole of each described bubble diffusing apparatus or the number of gas diffusion tube are 3-15, and is divided into multilayer and arranges.
4. flotation separation equipment as claimed in claim 3, it is characterized in that, each described bubble diffusing apparatus comprises 8 gas diffusion holes or gas diffusion tube, these 8 gas diffusion holes or gas diffusion tube are divided staggered two-layer up and down, 4 every layer, the angle between adjacent two gas diffusion holes of same layer or the gas diffusion tube is 90 °.
5. multistage flotation separation equipment as claimed in claim 2 is characterized in that, it is air compression plant that described wind send device.
6. multistage flotation separation equipment as claimed in claim 1 is characterized in that, described each board plug device also comprises fixing insertion.
7. multistage flotation separation equipment as claimed in claim 1 is characterized in that, each described flotation cells includes superposed cylindrical shell and is positioned at the tail ash gathering-device of bottom; Described board plug device consists of the part of described cylindrical shell barrel; The cone that described tail ash gathering-device is pointed end is bucket-shaped, and the outlet of described tail ash is positioned at the place, tip of described tail ash gathering-device bottom.
8. multistage flotation separation equipment as claimed in claim 7 is characterized in that, in each described flotation cells, the intersection of described cylindrical shell and described tail ash gathering-device is provided with filter.
9. multistage flotation separation equipment as claimed in claim 8 is characterized in that, each filter all is obliquely installed, and each filter is positioned at same inclined-plane; The height of described a plurality of bubble diffusing apparatus reduces to rear successively from first section.
10. multistage flotation separation equipment as claimed in claim 8 is characterized in that, each described filter all is horizontally disposed with, and each filter is positioned at same plane; Described each bubble diffusing apparatus height is consistent.
CN 201220360925 2012-07-24 2012-07-24 Plate -type coal ash multistage flotation separation equipment Expired - Fee Related CN202762553U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220360925 CN202762553U (en) 2012-07-24 2012-07-24 Plate -type coal ash multistage flotation separation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220360925 CN202762553U (en) 2012-07-24 2012-07-24 Plate -type coal ash multistage flotation separation equipment

Publications (1)

Publication Number Publication Date
CN202762553U true CN202762553U (en) 2013-03-06

Family

ID=47769157

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220360925 Expired - Fee Related CN202762553U (en) 2012-07-24 2012-07-24 Plate -type coal ash multistage flotation separation equipment

Country Status (1)

Country Link
CN (1) CN202762553U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102755934A (en) * 2012-07-24 2012-10-31 福建省龙岩龙能粉煤灰综合利用有限公司 Cell type multi-stage flotation separation equipment for coal ash
CN113546501A (en) * 2021-07-08 2021-10-26 山东竣鸿环保科技有限公司 High-quality fly ash production system and application thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102755934A (en) * 2012-07-24 2012-10-31 福建省龙岩龙能粉煤灰综合利用有限公司 Cell type multi-stage flotation separation equipment for coal ash
CN113546501A (en) * 2021-07-08 2021-10-26 山东竣鸿环保科技有限公司 High-quality fly ash production system and application thereof

Similar Documents

Publication Publication Date Title
CN102240608B (en) Coal ash flotation separation equipment provided with reflection cone gas dispersing device
CN102240610B (en) Self-gas supply mixed fly ash multistage flotation separation system
CN102755934B (en) Cell type multi-stage flotation separation equipment for coal ash
CN202762553U (en) Plate -type coal ash multistage flotation separation equipment
CN202113944U (en) Powdered coal ash floatation separating equipment with ultrasonic separating unit
CN202113946U (en) Coal ash flotation separation equipment with turbulent gas dispersing device
CN202199429U (en) Self-air supplying fly ash flotation separation system
CN202762555U (en) Pulverized fuel ash flotation separation device
WO2012167592A1 (en) Coal ashes flotation process and flotation equipment
CN202113945U (en) Powdered coal ash floatation separating equipment provided with conical diffusion area on tower wall
CN202151595U (en) Inner-inner tandem type fly ash flotation separation system
CN202173998U (en) Combined fly ash floatation separation system with self-air supply
CN102284370B (en) Turbulent current fly ash flotation process
CN102284375B (en) Pulverized fuel ash flotation separation equipment with physical separation device
CN202199430U (en) Internal cycle type fly ash flotation separation device
CN102728481B (en) Aerated coal ash flotation separation equipment
CN102773170B (en) Plug-flow aeration type fuel ash flotation separation equipment
CN202146823U (en) Inside-outside cascade type fly ash flotation separation system
CN202146824U (en) Outer-inner cascade type fly ash flotation-separation system
CN102319638B (en) Turbulent mixed pulverized fuel ash multi-stage floatation separation system
CN102284377B (en) Pulverized fuel ash flotation separation equipment with divergent cone
CN202151594U (en) Outside-outside cascading coal ash flotation separation system
CN2723031Y (en) Solid material screw separator
CN102284376B (en) Internal-internal fly ash multi-stage flotation separation system
CN102744154B (en) Aeration type coal ash flotation process

Legal Events

Date Code Title Description
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: 20130306

Termination date: 20170724

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