CN202752100U - Foam transferring pipeline structure of integration flotation system - Google Patents
Foam transferring pipeline structure of integration flotation system Download PDFInfo
- Publication number
- CN202752100U CN202752100U CN201220443232.0U CN201220443232U CN202752100U CN 202752100 U CN202752100 U CN 202752100U CN 201220443232 U CN201220443232 U CN 201220443232U CN 202752100 U CN202752100 U CN 202752100U
- Authority
- CN
- China
- Prior art keywords
- foam
- flotation cell
- low
- pipe
- low level
- 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 - Lifetime
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A foam transferring pipeline structure of an integration flotation system is composed of an upper-position flotation cell (1), an upper-position flotation cell foam chute (6), a low-position flotation cell (2), a low-position flotation cell foam chute (7), a foam overflow pipe (3), a mixed foam transferring pipe (4), a liquefaction foam transferring pipe (5) and a low-position flotation cell circulating pump inlet pipe (8). The upper-position end of the foam overflow pipe (3) is connected with the upper portion of the upper-position flotation cell foam chute (6), the low-position end of the foam overflow pipe (3) is connected with the low-position flotation cell foam chute (7), the upper-position end of the mixed foam transferring pipe (4) is connected with the middle portion of the upper-position flotation cell foam chute (6), the low-position end of the mixed foam transferring pipe (4) is connected with the low-position flotation cell (2), the upper-position end of the liquefaction foam transferring pipe (5) is connected with the bottom of the upper-position flotation cell foam chute (6), and the low-position end of the liquefaction foam transferring pipe (5) is connected with the low-position flotation cell circulating pump inlet pipe (8). The foam transferring structure is suitable to foam transferring of the integration flotation system and can obtain ideal flotation effects.
Description
Technical field
The integrated floatation system foam of this utility model transfer pipe structure belongs to ore processing flotation technology field, and the foam that the structure of this utility model is applicable to the integrated floatation system of microvesicle mineralising shifts, and can obtain more desirable flotation effect.
Background technology
Integrated floatation system is the floatation system of in recent years inventing, and traditional flotation mode is changed in this system, microvesicle mineralising flotation cell is integrated formed that flotation effect is good, flotation efficiency is high, save the brand-new flotation technology equipment of investment, energy efficient.This integrated floatation system has been applied for multinomial patent, mainly contains: 201020108249.1 1 kinds of efficient flotation separation integrated systems, 201020167495.4 Quick micro-bubble floatation integrated mechanisms, 201020177313.1 high-efficiency self-circulation flotation cells etc.This system has been widely used in the direct flotation of bauxite, the direct flotation process of apatite, obtained good effect, basically solved the flotation technology difficult problem of the ores such as bauxite, apatite, other various mineral especially oxide mineral have been had widely promotional value.
It is one of key technology of integrated floatation system that foam shifts, in the application in the past, usually the foam that is in high-order flotation cell generation is directly accessed the pump inlet pipe that is in the low level flotation cell, because foam is damaged liquefaction fully, and incomplete phenomenon is shifted in appearance, the situation of bubble operation also appears carrying secretly in circulating pump simultaneously, has aggravated cavitation erosion and the wearing and tearing of circulating pump.The integrated floatation system foam of this utility model transfer pipe structure has been utilized the grade otherness of foamover mineral just, the mineral that namely are not easy damaged foamover have the characteristic of higher grade, foam is divided into the liquefaction foam, mix-froth and overflow foam, and to the processing of classifying of three kinds of foams, the product bit comparison of liquefaction foamover mineral is low should to participate in refining process to obtain further purification, the grade of the mineral that mix-froth carries is placed in the middle, should participate in selected foam isolated chromatography layer obtains further to purify, the grade of ore of overflow foamover is basically near selected grade, do not need further selectedly, can directly be linked into selected Foam Flowing Groove.So not only solved the transhipment difficult problem of foam, so that the operation of integrated floatation system is simpler, moved more smooth simultaneously.
The content of utility model
The purpose of invention
The integrated floatation system foam of this utility model transfer pipe structure is invented for solving integrated floatation system foam branch problem.
Technical scheme
The integrated floatation system foam of this utility model transfer pipe structure is comprised of high-order flotation cell 1, high-order flotation cell Foam Flowing Groove 6, low level flotation cell 2, low level flotation cell Foam Flowing Groove 7, foam overflow pipe 3, mix-froth transfer pipeline 4, liquefaction foam transfer pipeline 5, low level flotation cell circulations pump inlet pipe 8; The high order end of foam overflow pipe 3 is connected with the top of high-order flotation cell Foam Flowing Groove 6, the low order end of foam overflow pipe 3 is connected with low level flotation cell Foam Flowing Groove 7, the high order end of mix-froth transfer pipeline 4 is connected with the middle part of high-order flotation cell Foam Flowing Groove 6, the low order end of mix-froth transfer pipeline 4 is connected with low level flotation cell 2, and the high order end of liquefaction foam transfer pipeline 5 and the bottom of high-order flotation cell Foam Flowing Groove 6 be connected, the liquefy low order end of foam transfer pipeline 5 is connected with low level flotation cell circulations pump inlet pipe 8.
During application, flotation froth in the high-order flotation cell Foam Flowing Groove 6 can be along foam overflow pipe 3, mix-froth transfer pipeline 4, liquefaction foam transfer pipeline 5, automatically flow into respectively waist, the low level flotation cell circulations pump inlet pipe 8 of low level flotation cell Foam Flowing Groove 7, low level flotation cell 2, enter refining process.
Beneficial effect
The integrated floatation system foam of this utility model transfer pipe structure has been utilized the grade otherness of foamover mineral just, the mineral that namely are not easy damaged foamover have the characteristic of higher grade, foam is divided into the liquefaction foam, mix-froth and overflow foam, and to the processing of classifying of three kinds of foams, the product bit comparison of liquefaction foamover mineral is low should to participate in refining process to obtain further purification, the grade of the mineral that mix-froth carries is placed in the middle, should participate in selected foam isolated chromatography layer obtains further to purify, the grade of ore of overflow foamover is basically near selected grade, do not need further selectedly, can directly be linked into selected Foam Flowing Groove.So not only solved the transhipment difficult problem of foam, so that the operation of integrated floatation system is simpler, moved more smooth simultaneously.
Description of drawings
Accompanying drawing 1 is the schematic diagram of the integrated floatation system foam of the utility model transfer pipe structure;
Such as accompanying drawing 1, the integrated floatation system foam of this utility model transfer pipe structure, formed by high-order flotation cell 1, high-order flotation cell Foam Flowing Groove 6, low level flotation cell 2, low level flotation cell Foam Flowing Groove 7, foam overflow pipe 3, mix-froth transfer pipeline 4, liquefaction foam transfer pipeline 5, low level flotation cell circulations pump inlet pipe 8; The high order end of foam overflow pipe 3 is connected with the top of high-order flotation cell Foam Flowing Groove 6, the low order end of foam overflow pipe 3 is connected with low level flotation cell Foam Flowing Groove 7, the high order end of mix-froth transfer pipeline 4 is connected with the middle part of high-order flotation cell Foam Flowing Groove 6, the low order end of mix-froth transfer pipeline 4 is connected with low level flotation cell 2, and the high order end of liquefaction foam transfer pipeline 5 and the bottom of high-order flotation cell Foam Flowing Groove 6 be connected, the liquefy low order end of foam transfer pipeline 5 is connected with low level flotation cell circulations pump inlet pipe 8.
During application, flotation froth in the high-order flotation cell Foam Flowing Groove 6 can be along foam overflow pipe 3, mix-froth transfer pipeline 4, liquefaction foam transfer pipeline 5, automatically flow into respectively waist, the low level flotation cell circulations pump inlet pipe 8 of low level flotation cell Foam Flowing Groove 7, low level flotation cell 2, enter refining process.
Embodiment
In the foam transfer pipe installation process of integrated floatation system, the top of the high order end of foam overflow pipe 3 with high-order flotation cell Foam Flowing Groove 6 is connected, the low order end of foam overflow pipe 3 is connected with low level flotation cell Foam Flowing Groove 7, the high order end of mix-froth transfer pipeline 4 is connected with the middle part of high-order flotation cell Foam Flowing Groove 6, the low order end of mix-froth transfer pipeline 4 is connected with low level flotation cell 2, and the high order end of liquefaction foam transfer pipeline 5 is connected with the bottom of high-order flotation cell Foam Flowing Groove 6, the low order end of liquefaction foam transfer pipeline 5 is connected with low level flotation cell circulations pump inlet pipe 8.The diameter of pipeline designs according to the foam flow.
Claims (1)
1. integrated floatation system foam transfer pipe structure is characterized in that integrated floatation system foam transfer pipe structure is comprised of high-order flotation cell (1), high-order flotation cell Foam Flowing Groove (6), low level flotation cell (2), low level flotation cell Foam Flowing Groove (7), foam overflow pipe (3), mix-froth transfer pipeline (4), liquefaction foam transfer pipeline (5), low level flotation cell circulations pump inlet pipe (8); The high order end of foam overflow pipe (3) is connected with the top of high-order flotation cell Foam Flowing Groove (6), the low order end of foam overflow pipe (3) is connected with low level flotation cell Foam Flowing Groove (7), the high order end of mix-froth transfer pipeline (4) is connected with the middle part of high-order flotation cell Foam Flowing Groove (6), the low order end of mix-froth transfer pipeline (4) is connected with low level flotation cell (2), and the high order end of liquefaction foam transfer pipeline (5) is connected with the bottom of high-order flotation cell Foam Flowing Groove (6), the low order end of liquefaction foam transfer pipeline (5) is connected with low level flotation cell circulations pump inlet pipe (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220443232.0U CN202752100U (en) | 2012-08-26 | 2012-08-26 | Foam transferring pipeline structure of integration flotation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220443232.0U CN202752100U (en) | 2012-08-26 | 2012-08-26 | Foam transferring pipeline structure of integration flotation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202752100U true CN202752100U (en) | 2013-02-27 |
Family
ID=47731295
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220443232.0U Expired - Lifetime CN202752100U (en) | 2012-08-26 | 2012-08-26 | Foam transferring pipeline structure of integration flotation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202752100U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551322A (en) * | 2013-10-29 | 2014-02-05 | 冯愚斌 | Skimmer |
| CN109158221A (en) * | 2018-08-23 | 2019-01-08 | 广东省大宝山矿业有限公司 | A kind of copper sulphur mine ore-sorting system improving foam pump mounting means |
-
2012
- 2012-08-26 CN CN201220443232.0U patent/CN202752100U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551322A (en) * | 2013-10-29 | 2014-02-05 | 冯愚斌 | Skimmer |
| CN103551322B (en) * | 2013-10-29 | 2015-07-01 | 冯愚斌 | Skimmer |
| CN109158221A (en) * | 2018-08-23 | 2019-01-08 | 广东省大宝山矿业有限公司 | A kind of copper sulphur mine ore-sorting system improving foam pump mounting means |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103301950B (en) | A kind of combination cation-collecting agent of hematite Counterfloatating desiliconization | |
| CN102302981A (en) | Beneficiation reagent and method for separating copper-molybdenum mixed concentrates | |
| CN104014431A (en) | Floatation process for oxidized coal slime | |
| CN202752100U (en) | Foam transferring pipeline structure of integration flotation system | |
| CN204824150U (en) | A continuous recovery processing device that is arranged in polycrystalline silicon production hydrogen chloride | |
| CN102179309A (en) | Foam controlling and flotation method for zinc oxide ore | |
| CN204342436U (en) | Utilize the reverse flotation system of the waste water process for processing phosphorus ore of phosphoric acid production line | |
| CN204338296U (en) | A kind of waste water can bypassing circulation utilize collophane direct reverse flotation production line | |
| CN204134756U (en) | A kind of novel deliming equipment | |
| CN204816851U (en) | Selectivity flocculation - post flotation recovery system of choice tailing of fine grain molybdenum | |
| CN203269834U (en) | System for separating starch from protein in corn primary pulp | |
| CN202778721U (en) | Micro-foam floatation tank body structure | |
| CN202921429U (en) | Novel flotation machine | |
| CN201953673U (en) | Water saving device of water-ring vacuum pump | |
| CN205361671U (en) | Chats discharge device of whirl - static microbubble flotation column | |
| CN204005937U (en) | Concentration pan cooling water recycling device | |
| CN207254026U (en) | A kind of purging sulfur dioxide system | |
| CN203916868U (en) | A kind ofly improve the ore-sorting system that slag gold recovery is soaked in arsenic-containing gold concentrate cyaniding | |
| CN204602418U (en) | Simple and easy agitation type flotation machine | |
| CN205076838U (en) | Full -automatic height dissolves tolerance air supporting system | |
| CN203803658U (en) | Boric acid and magnesium sulfate separating device | |
| CN204125501U (en) | A kind of energy-efficient mixing clarifying extraction equipment | |
| CN204569863U (en) | Pipeline coal transporting water delivery process unit under a kind of large drop ground potential condition | |
| CN204079563U (en) | A kind of cover pot type Water warfare flocculation tank | |
| CN202465401U (en) | Dual-circulating flow guide device with power generator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130227 |