CN202778723U - Multistage flotation column - Google Patents

Multistage flotation column Download PDF

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Publication number
CN202778723U
CN202778723U CN 201220402885 CN201220402885U CN202778723U CN 202778723 U CN202778723 U CN 202778723U CN 201220402885 CN201220402885 CN 201220402885 CN 201220402885 U CN201220402885 U CN 201220402885U CN 202778723 U CN202778723 U CN 202778723U
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CN
China
Prior art keywords
mozzle
flotation column
splitter
column
suction muffler
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 201220402885
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Chinese (zh)
Inventor
吴迪
吕红姿
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.)
SICHUAN VERTEX CONSTRUCTION CO Ltd
Original Assignee
SICHUAN VERTEX CONSTRUCTION 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 SICHUAN VERTEX CONSTRUCTION CO Ltd filed Critical SICHUAN VERTEX CONSTRUCTION CO Ltd
Priority to CN 201220402885 priority Critical patent/CN202778723U/en
Application granted granted Critical
Publication of CN202778723U publication Critical patent/CN202778723U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a multistage flotation column which solves the problems in the prior art that flotation efficiency of a center-split type flotation column is low and a special arranged liquid level monitoring device is not provided. The multistage flotation column comprises airflow guiding pipes (1), a separating column (2) which is arranged at the lower end of the airflow guiding pipe (1) and an airflow outlet (3) which is arranged at the lower end of the separating column (2). The dynamic fluidic type flotation column is characterized in that the upper end of the airflow guiding pipe (1) is provided with an air suction chamber (5) which is connected with the airflow guiding pipe (1) through a connecting pipe (4). The upper end of the air suction chamber (5) is provided with nozzle (6), wherein one end of the nozzle is inserted into the air suction chamber (5). The air suction chamber (5) is provided with an airflow inlet (7) which is communicated with external air pressure. The side wall of the separating column (2) is further provided with a liquid level sensor (8). The number of the airflow guiding pipes (1) is two. The two airflow guiding pipes are connected with the separating column (2) and horizontally arranged in a paratactic mode. The multistage flotation column has the advantages of being simple in structure, low in cost and convenient to achieve, and therefore suitable for popularization and utilization.

Description

The multistage flotation column
Technical field
The utility model relates to a kind of fine particle separation equipment, specifically, is a kind of multistage flotation column.
Background technology
Gu flotation is the method for carrying out liquid-liquid, solid-liquid and solid-separation (ore particle, oil droplet etc.) by the difference of the Surface Physical Chemistry character of particle; The method is with the running medium of bubble as particle.FLOTATION SEPARATION is to carry out in the floatation equipment of special use, and floatation equipment is mainly by following several: agitation impeller flotator, air flotation post and split type flotation column.At present, flotation column commonly used in the engineer operation is split type flotation column, and it has, and the flotation column height is low, the flotation efficiency advantages of higher; But through long-term experiment and practice, also there is following shortcoming in split type flotation device: inspiratory capacity is restricted, and ore pulp mixes abundant not with gas, and the mineralising effect is bad; And do not have ad hoc level control or watch-dog in the splitter, ore pulp often occurs and overflow, to such an extent as to have a strong impact on engineer operation.
The utility model content
The purpose of this utility model is to overcome defects, provide a kind of overall structure simple, realize easily floatation equipment.
To achieve these goals, the scheme of the utility model employing is as follows:
The multistage flotation column, comprise mozzle, be arranged on the splitter of this mozzle lower end, and the head piece that goes out that is arranged on the splitter lower end, be provided with the suction muffler that is attached thereto by tube connector in the upper end of described mozzle, this suction muffler upper end is provided with an end and inserts its inner nozzle, and offer the air flow inlet that communicates with ambient pressure at suction muffler, and on the sidewall of described splitter, also be provided with liquid level sensor, described mozzle number is two, and the two level is set up in parallel and all links to each other with splitter.
Further, described mozzle lower end tangentially links to each other with the splitter side.
Further, described air flow inlet number is more than one, and all is positioned at the upper end of suction muffler.
Further, described tube connector is 5 to 12 with the cross-sectional area ratio of mozzle.
The utility model compared with prior art has the following advantages and beneficial effect:
(1) the utility model is not only simple in structure, and with low cost, realization convenience;
(2) the utility model is provided with the suction muffler that is attached thereto by tube connector in the upper end of mozzle, this suction muffler upper end is provided with an end and inserts its inner nozzle, and offer the air flow inlet that communicates with ambient pressure at suction muffler, nozzle sprays high speed ore pulp with pressure, air flow velocity is little from the air flow inlet of suction muffler side is involved in, air and ore pulp jet enter tube connector and are taken away at a high speed by jet, thereby in suction muffler, form pseudo-vacuum state, and cause negative pressure, thereby more Air Entrainment is entered the jet operation area, it is gradually consistent when air arrives mozzle with ore pulp, and change the kinetic energy of fluid-mixing into pressure energy by mozzle, and air split be divided into minute bubbles, thereby form foam stream at mozzle; The breathing space of suction muffler is much larger than mozzle, and immobilized particles or oil droplet in the ore pulp and the minute bubbles split minute carry out sufficient mineralization at mozzle, guaranteed that effectively ore pulp is abundant with mixing of gas, its mixing efficiency is higher than traditional split type flotation column, mineralization is strong, and then has improved flotation efficiency;
(3) the utility model also is provided with liquid level sensor on the sidewall of splitter, and this liquid level sensor is connected with external attention device by holding wire, and it can monitor the height of liquid level in the splitter timely, has effectively avoided flow of slurry to overflow;
(4) so material is common common material on the market in the utility model, and it is simple in structure, low price, cost is very cheap, has established solid foundation for it promotes the use on a large scale;
(5) the mozzle number is two in the utility model, and the two level is set up in parallel and all links to each other with splitter, and according to actual needs, mozzle also can be set to three, four even more, and it is in order to improve flotation efficiency.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Wherein, the parts name that Reference numeral is corresponding is called: the 1-mozzle, and the 2-splitter, 3-goes out head piece, 4-tube connector, 5-suction muffler, 6-nozzle, 7-air flow inlet, 8-liquid level sensor.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing thereof the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment
As shown in Figure 1, the multistage flotation column, comprise mozzle 1, be arranged on the splitter 2 of this mozzle 1 lower end, and be arranged on splitter 2 lower ends go out head piece 3, be provided with the suction muffler 5 that is attached thereto by tube connector 4 in the upper end of described mozzle 1, these suction muffler 5 upper ends are provided with an end and insert its inner nozzle 6, and offer the air flow inlet 7 that communicates with ambient pressure at suction muffler 5.
The utility model also is provided with liquid level sensor 8 on the sidewall of splitter, this liquid level sensor 8 is connected with external attention device by holding wire, and it can monitor the height of liquid level in the splitter timely, has effectively avoided flow of slurry to overflow.
Mozzle 1 number is two in the utility model, and the two level is set up in parallel and all links to each other with splitter 2, and according to actual needs, mozzle 1 also can be set to three, four even more, and it is in order to improve flotation efficiency.
In the present embodiment, described mozzle 1 lower end tangentially links to each other with splitter 2 sides.
In order to improve air-breathing speed, described air flow inlet 7 numbers are more than one, and all are positioned at the upper end of suction muffler 5.
In the present embodiment, in order to guarantee ore pulp air pressure, described tube connector 4 is 5 to 12 with the cross-sectional area ratio of mozzle 1.
Principle of the present utility model: nozzle sprays high speed ore pulp with pressure, air flow velocity is little from the air flow inlet of suction muffler side is involved in, air and ore pulp jet enter tube connector and are taken away at a high speed by jet, thereby in suction muffler, form pseudo-vacuum state, and cause negative pressure, thereby more Air Entrainment is entered the jet operation area, it is gradually consistent when air arrives mozzle with ore pulp, and change the kinetic energy of fluid-mixing into pressure energy by mozzle, and air split be divided into minute bubbles, thereby form foam stream at mozzle; The breathing space of suction muffler is much larger than mozzle; and immobilized particles or oil droplet in the ore pulp and the minute bubbles split minute carry out sufficient mineralization at mozzle; guaranteed that effectively ore pulp is abundant with mixing of gas; its mixing efficiency is higher than traditional split type flotation column; mineralization is strong, and then has improved flotation efficiency.
According to above-described embodiment, can well realize the utility model.

Claims (4)

1. multistage flotation column, comprise mozzle (1), be arranged on the splitter (2) of this mozzle (1) lower end, and be arranged on splitter (2) lower end go out head piece (3), it is characterized in that: be provided with the suction muffler (5) that is attached thereto by tube connector (4) in the upper end of described mozzle (1), this suction muffler (5) upper end is provided with an end and inserts its inner nozzle (6), and offer the air flow inlet (7) that communicates with ambient pressure at suction muffler (5), and on the sidewall of described splitter (2), also be provided with liquid level sensor (8), wherein, described mozzle (1) number is two, and the two level is set up in parallel and all links to each other with splitter (2).
2. multistage flotation column according to claim 1, it is characterized in that: described mozzle (1) lower end tangentially links to each other with splitter (2) side.
3. multistage flotation column according to claim 2, it is characterized in that: described air flow inlet (7) number is more than one, and all is positioned at the upper end of suction muffler (5).
4. multistage flotation column according to claim 3 is characterized in that: described tube connector (4) is 5 to 12 with the cross-sectional area ratio of mozzle (1).
CN 201220402885 2012-08-15 2012-08-15 Multistage flotation column Expired - Fee Related CN202778723U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220402885 CN202778723U (en) 2012-08-15 2012-08-15 Multistage flotation column

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220402885 CN202778723U (en) 2012-08-15 2012-08-15 Multistage flotation column

Publications (1)

Publication Number Publication Date
CN202778723U true CN202778723U (en) 2013-03-13

Family

ID=47806067

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220402885 Expired - Fee Related CN202778723U (en) 2012-08-15 2012-08-15 Multistage flotation column

Country Status (1)

Country Link
CN (1) CN202778723U (en)

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130313

Termination date: 20130815