CN202246787U - Biological column leaching device - Google Patents
Biological column leaching device Download PDFInfo
- Publication number
- CN202246787U CN202246787U CN2011203362129U CN201120336212U CN202246787U CN 202246787 U CN202246787 U CN 202246787U CN 2011203362129 U CN2011203362129 U CN 2011203362129U CN 201120336212 U CN201120336212 U CN 201120336212U CN 202246787 U CN202246787 U CN 202246787U
- Authority
- CN
- China
- Prior art keywords
- inner core
- cylindrical
- external jacket
- utility
- model
- 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.)
- Withdrawn - After Issue
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The utility model relates to a biological column leaching device for leaching metal in ores and belongs to biohydrometallurgy mechanical equipment. The lower part of an outer clamping sleeve of the biological column leaching device provided by the utility model is provided with a support; the bottom of the outer clamping sleeve is provided with an air inlet, a material discharging port and a sampling port; a base plate is fixedly installed on the support, and is provided with a ventilation hole; the ventilation hole is provided with a cylindrical ventilation pipe the top of which is closed; the pipe wall of the cylindrical ventilation pipe is provided with small holes; the base plate of an inner cylinder is provided with a through hole; the inner cylinder is arranged in the outer clamping sleeve; the cylindrical ventilation pipe passes through the through hole and is arranged in the inner cylinder; the top of the inner cylinder is provided with an end cover; the top of the end cover is provided with an opening; and the inner cylinder and the end cover are fixedly connected through a bolt. According to the utility model, the ventilation quantity in a liquid is increased through the cylindrical ventilation pipe, so that the introduced gas can be better distributed in ore pulp, and the microganism growth and metabolism capability is improved, thus the ore pulp utilization ratio is improved. The biological column leaching device provided by the utility model has the advantages of simple structure, uniform solid and liquid mixture, full ventilation dissolution, less blocking possibility for the ore pulp and the like.
Description
Technical field
The utility model relates to a kind of biological post bath unit, is used for the leaching of ore metal, belongs to the biological metallurgy mechanical means.
Background technology
The distinguishing feature of Mineral Resources in China is that low, complicated, the hard to manage and middle-size and small-size ore deposit of grade is in the majority, and traditional dressing and smelting process is difficult to carry out economy, green, extracts effectively." national medium-term and long-term scientific and technical development program strategic research " pointed out " Mineral Resources in China is in short supply, and situation is serious ".Solve Mineral Resources in China problem in short supply, just must the efficient new technology of utilizing of development resource.
Research and production practice both at home and abroad show; Compare traditional metallurgical technology; The biological metallurgy technology demonstrates powerful advantages, and in the development and use of low-grade, complicated, unmanageable Mineral resources, biological metallurgy has low cost, short flow process, pollutes advantages such as little; Become the cutting edge technology of 21 century world's mineral extraction, have broad application prospects.
That is that all right is ripe for technical application among this development, and have many weak points: single bacterium oxidation capacity that one of which, biological metallurgy are used has not had obvious raising, needs to optimize bacterial growth condition equal angles and improve whole bacterial oxidation ability from promoting bacterial biomass; Its two, high-grade ore is biological to leach that the bio-reactor ubiquity shearing force of industrial application is big, the pair cell damage is serious, pulp density is low causes the device processes ability not high.
Post bath unit in practical application is commonly the jar of vertical barrel type at present, and the breather device is simple, and ore pulp mixes inhomogeneous, causes leaching effect bad, the not high shortcoming of efficient.
Therefore, the high-performance bio of exploitation with efficient mixed performance and good oxygen mass transfer coefficients leaches that reactor drum is used to increase leaching yield, shortening leaching cycle, reducing production costs just seems particularly important.
Leach in the device in prior biological; All there is certain weak point; Such as the multiple guide shell gas circulating bioreactor bacteria ore leaching of Lin Jianqun etc. with soak the ore deposit bacterium and cultivate (the patent No.: 200610070171.7); Pay attention to soaking the effect of ventilating in the process of ore deposit, utilize ventilation to reach the purpose of stirring.But in soaking the ore deposit process, when ventilation was excessive, the shearing force that ventilation produces was very big to the growth metabolism influence of soaking the ore deposit bacterium; And a kind of microbial column type leaching reactor of Zhou Hongbo etc. (patent No.: 200910310522.0) pay attention to control and circulation to the reaction conditions in the reaction process, make the production cost that soaks the ore deposit raise; And a kind of microbial leaching device of Huo Qiang etc. (patent No.: 200720169742.2) pay attention to soak in the reactor drum circulation of bacterium liquid, to the requirement of ventilation with utilize not high.
The utility model content
The purpose of the utility model is to provide a kind of can make solid-liquid thorough mixing more, improves the bioleaching device of metal leaching rate.
Technical solution:
The utility model comprises: external jacket, inner core, and the external jacket bottom is provided with bearing, and the bottom is provided with inlet mouth, drain hole and thief hole; Be installed with base plate on the bearing, base plate is provided with ventilating pit, and ventilating pit is provided with cylindrical ventpipe; Cylindrical ventpipe top seal, tube wall is provided with aperture, and the base plate of inner core is provided with through hole; Inner core places in the external jacket, and cylindrical ventpipe passes through hole and places in the inner core, and the inner core top is provided with end cap; The end cap top is provided with opening, and inner core is connected through bolt with end cap.
Said external jacket is cylindrical tubular.
Said external jacket bottom is the spherical end.
The contact position of said external jacket top and inner core is provided with seal ring, and inner core can slide up and down along external jacket.
Said external jacket inwall is provided with secondary bearing.
Said secondary bearing is provided with spring.
The utility model adopts inside and outside double-jacket, and certain hour utilizes mechanical force to promote inner core at interval, makes ore pulp partly flow into external jacket and carries out the mixing of secondary ore pulp, increases the solid-liquid contact area with this.The utility model also increases the air flow in the liquid through cylindrical ventpipe, and the gas that helps feeding is distributed in the ore pulp better, improves the microorganism growth metabolic capacity, thereby improves the utilization ratio of ore pulp.The utility model is than the conventional post bath unit, have simple in structure, solid-liquid mixes, ventilate dissolving fully, advantages such as ore pulp prevented from caking.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the vertical view at the A-A place of the utility model Fig. 1;
Fig. 3 the utility model B place enlarged view;
The cylindrical ventpipe enlarged diagram of Fig. 4 the utility model.
Embodiment
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, the utility model is applicable to that the biology of various metals in the biological metallurgy leaches, and this device comprises three main parts, external jacket 5, inner core 8 and cylindrical ventpipe 7.
The device of the utility model is processed by the acid and alkali-resistance corrosion-resistant material, installs changeablely, is used for breadboard packaged unit and can adopts manufacturings such as synthetic glass or speciality plastics, and large-scale plant can adopt the stainless material manufacturing through special processing.
This device forms the effect of similar stirring through the mutual motion of inside and outside chuck, reaches the well-mixed purpose of ore pulp; Through the effect of cylindrical ventpipe, make the required ventilation of growth metabolism of thalline meet the requirements of level, and ventilation can be on certain degree mixed ore pulp once more, reduce the compacting, caking of ore pulp etc.Reach the increase leaching yield through changing the microbial growth environmental aspect, shorten the purpose of production cycle.
The utility model practical implementation process is following:
After the utility model carries out the high-temperature steam sterilization to device; Under aseptic condition, open the spherical end cap 2 of inner core 8; The ore that adds certain grain size; Inner core 8 loam cakes and inner core cylindrical part are sealed to prevent microbiological contamination; With pump a certain amount of bacterium liquid of finite concentration is pumped into the inner core 8 from opening 1 again, bacterium liquid is mixed with ore; The temperature of setting device, PH make device be in the metabolic environmental optima of microorganism growth; After reaction for some time inner core 8 liftings once are put on first secondary bearing 15; Again inner core 8 liftings once are put on the next secondary bearing 15 after reacting for some time again; Promote so repeatedly, up to rising on last secondary bearing 15 behind the reaction certain hour, reaction finishes; This moment, ore pulp was positioned at external jacket 5 fully, opened external jacket bottom drain hole 16, emitted the extraction that ore pulp is used for follow-up metal; Once soak all processes in ore deposit thereby accomplish.
Introduce a kind of instance of laboratory applications the utility model below:
The device TV is 50L, and the work loading amount is 35L; Device external jacket column part height is 1000mm, and diameter is 300mm; Device inner core column part height is 1000mm, and diameter is 260mm.
Gold mine is husky: granularity is 200 orders, and Gold Content is 46g/t.
Bacterial classification is had a liking for the ferrous thiobacillus of acid oxidase (Acidithiobacillus ferrooxidans).
Strain preparation and inoculation are had a liking for the ferrous thiobacillus of acid oxidase (Acidithiobaci1lus ferrooxidans) and are cultivated the improved 9K substratum of employing, and 500ml triangular flask liquid amount is 200ml; 30 ℃, PH is 2.0, and shaking table is 160r/min; Be cultured to logarithmic phase; Inoculation, inoculum size is 8%, from the charging opening adding inner core of inner core.
Improved 9K substratum: (NH
4)
2SO
43g, KCl 0.1g, K
2HPO
40.5g, MgSO
4H
2O 0.5g, 0.01g, Ca (NO
3) 20.01g, zero(ppm) water 1000mL, pH 2.0.On the basis of improved 9K substratum, add ferrous sulfate 44.2g/L.
Soak the ore deposit condition: 8% pulp density, PH are 2.0, and temperature is 30 ℃, and air flow is 1.8m
3/ h adopts the single-stage batch operation mode.
Sampling regularly detects bacterium liquid, with the content of atomic fluorescence spectrum mensuration arsenic, with the content of barium sulfate turbidimetry mensuration sulfate radical, measures Fe with dichromate titration
2+Oxidation ratio, survey the concentration of thalline with ultraviolet spectrophotometer.
Be 30d reaction time, is reacted to the 5th day and promotes an inner core, is reacted to the 10th day and promotes an inner core, is reacted to the 20th day and promotes an inner core.Recording arsenic-removing rate behind the 30d is 75.6%.
Claims (6)
1. biological post bath unit is characterized in that, comprising: external jacket (5), inner core (8); External jacket (5) bottom is provided with bearing (11), and the bottom is provided with thief hole (12), inlet mouth (13), drain hole (16), is installed with base plate (14) on the bearing (11); Base plate (14) is provided with ventilating pit, and ventilating pit is provided with cylindrical ventpipe (7), cylindrical ventpipe (7) top seal; Tube wall is provided with aperture (17), and the base plate (9) of inner core (8) is provided with through hole (10), and inner core (8) places in the external jacket (5); Cylindrical ventpipe (7) passes through hole (10) and places in the inner core (8); Inner core (8) top is provided with end cap (2), and end cap (2) top is provided with opening (1), and inner core (8) is fixedly connected through bolt (3) with end cap (2).
2. biological post bath unit according to claim 1 is characterized in that said external jacket (5) is cylindrical tubular.
3. biological post bath unit according to claim 1 and 2 is characterized in that, said external jacket (5) bottom is the spherical end (6).
4. biological post bath unit according to claim 3 is characterized in that, the contact position of said external jacket (5) top and inner core (8) is provided with seal ring, and inner core (8) can slide up and down along external jacket (5).
5. biological post bath unit according to claim 4 is characterized in that, said external jacket (5) inwall is provided with secondary bearing (15).
6. biological post bath unit according to claim 5 is characterized in that said secondary bearing (15) is provided with spring.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203362129U CN202246787U (en) | 2011-08-30 | 2011-08-30 | Biological column leaching device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203362129U CN202246787U (en) | 2011-08-30 | 2011-08-30 | Biological column leaching device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202246787U true CN202246787U (en) | 2012-05-30 |
Family
ID=46108058
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011203362129U Withdrawn - After Issue CN202246787U (en) | 2011-08-30 | 2011-08-30 | Biological column leaching device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202246787U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102277490A (en) * | 2011-08-30 | 2011-12-14 | 内蒙古科技大学 | Biological column leaching device |
CN102703687A (en) * | 2012-06-15 | 2012-10-03 | 东华大学 | Temperature controllable device for selectively leaching minerals by bacteria |
CN106636636A (en) * | 2016-11-03 | 2017-05-10 | 长春黄金研究院 | Microbubble strengthened biological oxidation pretreatment method for gold concentrate difficult to deal with |
-
2011
- 2011-08-30 CN CN2011203362129U patent/CN202246787U/en not_active Withdrawn - After Issue
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102277490A (en) * | 2011-08-30 | 2011-12-14 | 内蒙古科技大学 | Biological column leaching device |
CN102277490B (en) * | 2011-08-30 | 2013-05-29 | 内蒙古科技大学 | Biological column leaching device |
CN102703687A (en) * | 2012-06-15 | 2012-10-03 | 东华大学 | Temperature controllable device for selectively leaching minerals by bacteria |
CN102703687B (en) * | 2012-06-15 | 2014-02-26 | 东华大学 | Temperature controllable device for selectively leaching minerals by bacteria |
CN106636636A (en) * | 2016-11-03 | 2017-05-10 | 长春黄金研究院 | Microbubble strengthened biological oxidation pretreatment method for gold concentrate difficult to deal with |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101333599A (en) | Cyanidation aurum-extracting method for preprocessing high-arsenic complex refractory gold ore by oxidation with arsenic resistant strains | |
CN101016584A (en) | Multiple guide shell gas circulating bioreactor bacteria ore leaching and ore leaching bacteria culture | |
CN202246787U (en) | Biological column leaching device | |
CN102277490B (en) | Biological column leaching device | |
CN102002588A (en) | Bioleaching method-uranium leaching from fungus | |
CN109628357A (en) | A kind of ferrous oxide complex microbial inoculum and its application | |
CN104561544A (en) | Light-intensified bioleaching method for semiconductor minerals | |
CN102127638B (en) | Biological reaction device and method for stably outputting Fe<3+> | |
CN103805777B (en) | Method of strengthening microbiological leaching of pyrites | |
CN108285980A (en) | The method of metal in inorganic Ore Leaching-bioleaching collaboration recycling lithium ion battery | |
Dan et al. | Reductive leaching of manganese from manganese dioxide ores by bacterial-catalyzed two-ores method | |
CN101298640B (en) | Biological-chemical dipolar reactor leaching process | |
CN103305553A (en) | Biological resourceful treatment method for ferrous sulfate | |
CN107858507B (en) | A kind of complex method improving sulfur oxidizing bacterium kind Chalcopyrite Leaching efficiency | |
CN101392327B (en) | Method for leaching copper in waste printed circuit board by microbiology | |
CN104531990A (en) | Biological gold extraction process of antimony-bearing complex refractory gold ore and microorganism used in same | |
CN203613183U (en) | Vertical solid-state fermentation/self-circulation cooling/distillation integrated device | |
CN107119188B (en) | A method of manganese in manganese oxide ore is extracted based on molten release of nitrococcus reduction-diluted acid | |
CN102020252A (en) | Biological leaching method of low-grade tellurium mine | |
CN101899570B (en) | Preoxidation treating method for leaching arsenic golden ores by using drum type reactor organisms | |
CN104004909B (en) | Utilize the method and apparatus of metallurgical microbe-preoxidation gold golden ore concentrate hard to treat | |
CN103060554B (en) | Vertical cell immobilized reactor for producing ferric irons by biological oxidation | |
RU2560627C2 (en) | Method of leaching of valuable components and rare-earth elements from cinder material | |
CN109182751B (en) | A method of chalcopyrite Bioleaching is promoted based on iron sulphur metabolic regulation | |
Rasoulnia et al. | High-rate and-yield continuous fluidized-bed bioconversion of glucose-to-gluconic acid for enhanced metal leaching |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20120530 Effective date of abandoning: 20130529 |
|
RGAV | Abandon patent right to avoid regrant |