CN102161015A - Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor - Google Patents
Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor Download PDFInfo
- Publication number
- CN102161015A CN102161015A CN2011100627014A CN201110062701A CN102161015A CN 102161015 A CN102161015 A CN 102161015A CN 2011100627014 A CN2011100627014 A CN 2011100627014A CN 201110062701 A CN201110062701 A CN 201110062701A CN 102161015 A CN102161015 A CN 102161015A
- Authority
- CN
- China
- Prior art keywords
- microbiological oxidation
- ore pulp
- oxidation reactor
- foam
- microbiological
- 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.)
- Granted
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 invention discloses a bubble treatment method of a flotation gold concentrate microbiological oxidation pretreatment process and a microbiological oxidation reactor. The method comprises the following steps of: arranging a bubble baffle plate at an ore pulp overflow port in the microbiological oxidation reactor to keep bubbles floating on the surface of ore pulp in the microbiological oxidation reactor, wherein only the ore pulp on the lower part of an ore liquid level can flow to the next microbiological oxidation reactor; and spraying an antifoaming agent to the bubbles floating on the surface of the ore pulp in the microbiological oxidation reactor to convert the bubbles into the ore pulp, so that the ore pulp and the ore pulp in the microbiological oxidation reactor are microbiologically oxidized together, the flotation gold concentrate microbiological oxidation pretreatment is completely performed, and the gold recovery rate is improved. The microbiological oxidation reactor has a structure that: an antifoaming agent spraying system inserted into the body of the microbiological oxidation reactor is arranged on the upper part of the reactor; and the bubble baffle plate is arranged at the ore pulp overflow port in the microbiological oxidation reactor.
Description
Technical field
The present invention relates to a kind of foam processing method and microbiological oxidation reactor of gold floatation concentrate microbiological oxidation pretreating process, this method utilizes foam baffle that the foam that produces in the gold floatation concentrate microbiological oxidation preprocessing process is retained in the microbiological oxidation reactor, destroy foam by adding surfactant then, foam is transformed into ore pulp, the ore pulp that makes it in the microbiological oxidation reactor carries out microbiological oxidation, finally reach gold floatation concentrate microbiological oxidation preliminary treatment purpose completely, improve the rate of recovery of gold.
Background technology
Rapid exploitation along with the mining industry resource, reduce day by day in tractable gravel mine and the lode gold ore deposit of easily soaking, gold is in the microfine package status type difficult-treating gold mine and contains arsenic and sulphur, and gold floatation concentrate microbiological oxidation preconditioning technique is to solve the difficult-treating gold mine resource in recent years to reclaim one of effective means of gold.China is in world lead level at present in this technical field.Gold floatation concentrate microbiological oxidation preconditioning technique promptly is in gold floatation concentrate ore pulp system, utilizes the characteristics of mineral such as having a liking for sour oxygen consumption microbiological oxidation dissolving arsenic, sulphur, iron, sulfide is wrapped up gold be transformed into exposure and can soak gold, reaches the final purpose that reclaims gold.In the microbiological oxidation process, be to supply with a large amount of air in the microbiological oxidation reactor to be absolutely necessary to gold floatation concentrate ore pulp system.But, because gold floatation concentrate is many based on sulfide, belong to the floatability mineral, understand residual a large amount of floating agent in addition in the gold floatation concentrate, the Gold Concentrate under Normal Pressure that particularly newly floatingly selects, floating agent almost all is retained in the gold floatation concentrate, so, just can produce mineralization during air supply in the microbiological oxidation process, and then producing a large amount of gold floatation concentrate foams, this floatation of foam can't be finished microbiological oxidation in microbiological oxidation reactor ore pulp surface, and can go downstream along with ore pulp flows, enter pretreated other operation of microbiological oxidation; When serious, the foam of generation can be gone out from the microbiological oxidation reactor in overflow, " the emitting groove " that promptly is commonly called as, and above-mentioned phenomenon can cause gold floatation concentrate microbiological oxidation deleterious when taking place, and influences the high efficiente callback of subsequent job gold; During especially severe, floating foam can adsorb a large amount of simple substance gold, causes bigger gold loss.At present, common treating method is: gold floatation concentrate is carried out airing, volatilization floating agent wherein; Or strengthen the washup operation in the grinding process before the gold floatation concentrate microbiological oxidation, remove floating agent.But, above-mentioned treating method all can not solve the flotation froth problem that produces in the microbiological oxidation process well, can only be on generation, to control, the problem of bringing is to make gold floatation concentrate microbiological oxidation pretreating process complicated, increased production process, sometimes even can cause the loss of gold floatation concentrate, the washup operation will have been wasted great amount of water resources, generation contains organic wastewater in a large number, does not add improvement and also can cause environmental pollution.
Summary of the invention
The foam processing method and the microbiological oxidation reactor that the purpose of this invention is to provide a kind of gold floatation concentrate microbiological oxidation pretreating process, the present invention's method is that the foam that will produce in the gold floatation concentrate microbiological oxidation process is retained in foam in the microbiological oxidation reactor by the foam baffle way is set, spray defoamer to foam then, by defoamer foam is eliminated, be transformed into ore pulp, carry out microbiological oxidation with ore pulp in the microbiological oxidation reactor, the final gold floatation concentrate of realizing, floating agents etc. are oxidation Decomposition all, the gold in the high efficiente callback difficult-treating gold mine resource.
The step of the present invention's method is as follows:
(1): the ore pulp overfall place in the microbiological oxidation reactor is provided with foam baffle, and the foam that floats on the ore pulp surface is retained in the microbiological oxidation reactor, has only the ore pulp of liquid level bottom, ore deposit just can flow in the next stage microbiological oxidation reactor.
Usually the ore pulp in the microbiological oxidation reactor flows automatically in the next stage microbiological oxidation reactor by outlet in surface stream mode.The present invention is provided with a foam baffle at microbiological oxidation reactor ore pulp overfall place, and the foam that floats on the ore pulp surface is retained in the microbiological oxidation reactor, has only the ore pulp of liquid level bottom, ore deposit just can flow in the next stage microbiological oxidation reactor.The ore pulp that flows in the next stage microbiological oxidation reactor may carry the small part floating agent, and still, the microbiological oxidation reactor that foam baffle is set by what just can thoroughly solve in the microbiological oxidation process and produce bubble-related issues.
(2): the foam to microbiological oxidation reactor ore pulp surface flotation sprays defoamer.
The purpose of spraying defoamer is exactly to eliminate floating foam, make foam be transformed into ore pulp, and then the ore pulp in the microbiological oxidation reactor carries out microbiological oxidation.
How much intensity of sprinkling defoamer decides on buoyant foam, generally is as the criterion to expose the ore pulp surface behind the froth breaking.
The body interior of microorganism used therefor oxidation reactor of the present invention has the air feed distributor, the upper part of body side is provided with the ore pulp overfall, the ore pulp overfall is connected with ore pulp from chute, the inside of body is provided with stirring system, upper part of body is provided with the defoamer sprinkling system of inserting to body interior, and body interior is positioned at ore pulp overfall place and is provided with foam baffle.
The invention has the beneficial effects as follows: the present invention's method is in the microbiological oxidation reactor, stop foam by foam baffle is set, then, eliminate foam by spraying defoamer again, finally make gold floatation concentrate microbiological oxidation preliminary treatment complete, improved gold recovery.
Description of drawings
Fig. 1 is the structural representation of microorganism used therefor oxidation reactor of the present invention.
The specific embodiment:
See also shown in Figure 1, structural representation for microorganism used therefor oxidation reactor 1 of the present invention, the body interior of microbiological oxidation reactor 1 wherein has air feed distributor 2, the upper part of body side is provided with ore pulp overfall 3, ore pulp overfall 3 is connected with ore pulp from chute 4, the inside of body is provided with stirring system 8, and upper part of body is provided with the defoamer sprinkling system 7 of inserting to body interior, and body interior is positioned at ore pulp overfall 3 places and is provided with foam baffle 5.
Cooperate shown in Figure 1ly, the step of the present invention's method is as follows:
(1): ore pulp overfall 3 places in microbiological oxidation reactor 1 are provided with foam baffle 5, the foam 6 that floats on the ore pulp surface is retained in the microbiological oxidation reactor 1, has only the ore pulp of liquid level bottom, ore deposit just can flow in the next stage microbiological oxidation reactor.
Usually the ore pulp in the microbiological oxidation reactor 1 flows automatically in the next stage microbiological oxidation reactor by outlet in surface stream mode.The present invention is provided with a foam baffle 5 at microbiological oxidation reactor 1 ore pulp overfall 3 places, and the foam 6 that floats on the ore pulp surface is retained in the microbiological oxidation reactor 1, has only the ore pulp of liquid level bottom, ore deposit just can flow in the next stage microbiological oxidation reactor.The ore pulp that flows in the next stage microbiological oxidation reactor may carry the small part floating agent, and still, the microbiological oxidation reactor 1 that foam baffle 5 is set by what just can thoroughly solve in the microbiological oxidation process and produce bubble-related issues.
(2): the foam 6 to microbiological oxidation reactor 1 ore pulp surface flotation sprays defoamer.
The purpose of spraying defoamer is exactly to eliminate floating foam 6, make foam 6 be transformed into ore pulp, and then the ore pulp in microbiological oxidation reactor 1 carries out microbiological oxidation.
How much intensity of sprinkling defoamer decides on buoyant foam 6, generally is as the criterion to expose the ore pulp surface behind the froth breaking.
Claims (2)
1. the foam processing method of a gold floatation concentrate microbiological oxidation pretreating process, the step of this method is as follows:
(1): the ore pulp overfall place in the microbiological oxidation reactor is provided with foam baffle, and the foam that floats on the ore pulp surface is retained in the microbiological oxidation reactor, has only the ore pulp of liquid level bottom, ore deposit just can flow in the next stage microbiological oxidation reactor;
(2): the foam to microbiological oxidation reactor ore pulp surface flotation sprays defoamer, make foam be transformed into ore pulp, and then the ore pulp in the microbiological oxidation reactor carries out microbiological oxidation.
2. employed microbiological oxidation reactor of the described method of claim 1, the body interior of its microbiological oxidation reactor (1) has air feed distributor (2), the upper part of body side is provided with ore pulp overfall (3), ore pulp overfall (3) is connected with ore pulp from chute (4), the inside of body is provided with stirring system (8), it is characterized in that: upper part of body is provided with the defoamer sprinkling system (7) of inserting to body interior, and body interior is positioned at ore pulp overfall (3) and locates to be provided with foam baffle (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100627014A CN102161015B (en) | 2011-03-16 | 2011-03-16 | Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100627014A CN102161015B (en) | 2011-03-16 | 2011-03-16 | Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102161015A true CN102161015A (en) | 2011-08-24 |
| CN102161015B CN102161015B (en) | 2013-04-03 |
Family
ID=44462627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011100627014A Active CN102161015B (en) | 2011-03-16 | 2011-03-16 | Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102161015B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285625A (en) * | 2013-06-13 | 2013-09-11 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103433143A (en) * | 2013-09-17 | 2013-12-11 | 长沙有色冶金设计研究院有限公司 | Calin type gold ore flotation method |
| CN104831059A (en) * | 2015-04-12 | 2015-08-12 | 长春黄金研究院 | Horizontal microbial oxidation reactor |
| CN105537006A (en) * | 2016-02-02 | 2016-05-04 | 青岛智瑞生物有限公司 | Method for achieving flotation of gold-containing ores through biological agent |
| CN105925798A (en) * | 2016-05-25 | 2016-09-07 | 长春黄金研究院 | Microorganism metallurgical reactor suitable for extremely cold environment |
| CN106378266A (en) * | 2016-11-01 | 2017-02-08 | 长春黄金研究院 | Foam treating device and method for microorganism oxidation pretreatment for flotation gold concentrate |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4816234A (en) * | 1985-05-10 | 1989-03-28 | Kamyr, Inc. | Utilization of oxygen in leaching and/or recovery procedures employing carbon |
| CN1097357A (en) * | 1993-06-10 | 1995-01-18 | 张怀信 | Eliminate the method for flotation concentrate mineralized froth |
| US20010002312A1 (en) * | 1996-10-04 | 2001-05-31 | Sharp James E. | Rapid ferrous sulfate biooxidation |
| CN1387581A (en) * | 1999-09-07 | 2002-12-25 | 比利顿知识产权有限公司 | Bioleaching of sulphide minerals |
| CN101285118A (en) * | 2008-05-20 | 2008-10-15 | 华东理工大学 | Biologic oxidation reactor for refractory auric sulfide ore |
| CN101961684A (en) * | 2010-07-16 | 2011-02-02 | 曹树营 | Overflow type enhanced tailing jet flow flotation device |
-
2011
- 2011-03-16 CN CN2011100627014A patent/CN102161015B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4816234A (en) * | 1985-05-10 | 1989-03-28 | Kamyr, Inc. | Utilization of oxygen in leaching and/or recovery procedures employing carbon |
| CN1097357A (en) * | 1993-06-10 | 1995-01-18 | 张怀信 | Eliminate the method for flotation concentrate mineralized froth |
| US20010002312A1 (en) * | 1996-10-04 | 2001-05-31 | Sharp James E. | Rapid ferrous sulfate biooxidation |
| CN1387581A (en) * | 1999-09-07 | 2002-12-25 | 比利顿知识产权有限公司 | Bioleaching of sulphide minerals |
| US6860919B1 (en) * | 1999-09-07 | 2005-03-01 | Billiton Intellectual Property, B.V. | Recovery of precious metal from sulphide minerals by bioleaching |
| CN101285118A (en) * | 2008-05-20 | 2008-10-15 | 华东理工大学 | Biologic oxidation reactor for refractory auric sulfide ore |
| CN101961684A (en) * | 2010-07-16 | 2011-02-02 | 曹树营 | Overflow type enhanced tailing jet flow flotation device |
Non-Patent Citations (1)
| Title |
|---|
| 方兆珩: "生物氧化浸矿反应器的研究进展", 《黄金科学技术》, vol. 10, no. 06, 30 December 2002 (2002-12-30), pages 1 - 7 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285625A (en) * | 2013-06-13 | 2013-09-11 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103285625B (en) * | 2013-06-13 | 2015-08-26 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103433143A (en) * | 2013-09-17 | 2013-12-11 | 长沙有色冶金设计研究院有限公司 | Calin type gold ore flotation method |
| CN104831059A (en) * | 2015-04-12 | 2015-08-12 | 长春黄金研究院 | Horizontal microbial oxidation reactor |
| CN105537006A (en) * | 2016-02-02 | 2016-05-04 | 青岛智瑞生物有限公司 | Method for achieving flotation of gold-containing ores through biological agent |
| CN105537006B (en) * | 2016-02-02 | 2018-04-24 | 青岛智瑞生物有限公司 | Using the method for biological agent flotation gold containing ore |
| CN105925798A (en) * | 2016-05-25 | 2016-09-07 | 长春黄金研究院 | Microorganism metallurgical reactor suitable for extremely cold environment |
| CN106378266A (en) * | 2016-11-01 | 2017-02-08 | 长春黄金研究院 | Foam treating device and method for microorganism oxidation pretreatment for flotation gold concentrate |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102161015B (en) | 2013-04-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102161015B (en) | Bubble treatment method of flotation gold concentrate microbiological oxidation pretreatment process and microbiological oxidation reactor | |
| CN104944656B (en) | Method and device for pretreating high-concentration wastewater through ultraviolet-ozone co-oxidation | |
| CN105585177A (en) | Desulfurization wastewater softening device and method | |
| CN103521347A (en) | Method for separating copper-molybdenum mixed concentrate high in secondary copper content | |
| CN103290715B (en) | Waste paper deinking process and apparatus thereof | |
| CN103521357A (en) | Method for utilizing return water of separation flotation for copper and molybdenum bulk concentrates | |
| CN103752414A (en) | Pulp mixing reinforced deep flotation technology process | |
| CN109550597A (en) | A kind of adjustable copper-cobalt ore method for floating for the treatment of capacity | |
| CN103146920A (en) | Pretreatment method for refractory gold ore containing arsenic and sulfur | |
| CN102502934A (en) | Treatment chemical for lead-zinc flotation tailing wastewater | |
| CN113247982B (en) | High-sulfur wastewater recycling treatment method and system | |
| CN109365141B (en) | Coal slime flotation process with recycling flotation agent | |
| CN205367958U (en) | Remaining hydrogen peroxide's device in rapid elimination waste water | |
| CN106669980B (en) | A kind of method for separating of the microfine oxidized coal slime based on colloid bubble | |
| CN113019708A (en) | Oxidation flotation separation process for copper-molybdenum bulk concentrate | |
| CN203320327U (en) | Waste paper deinking device | |
| CN106702387A (en) | On-line alkaline ammonium sulfate etching waste liquid cyclic regeneration system | |
| CN204039189U (en) | Micro-etched waste liquid and low copper waste water copper recovery system | |
| CN106636636A (en) | Microbubble strengthened biological oxidation pretreatment method for gold concentrate difficult to deal with | |
| CN110342688A (en) | The method that waste acid integrated use is handled in cyanogen slag harmlessness | |
| CN105177287A (en) | Method for desorption and gold extraction in flotation technology | |
| CN203715410U (en) | Device for treating pulping wastewater via Fenton catalytic oxidation method | |
| CN107188345A (en) | White tungsten ore dressing vacuum in draft tube technique | |
| CN204607581U (en) | A kind of acid-restoring plant of lead acid cell | |
| CN203360135U (en) | Coking desulfurization waste liquid pretreatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 130012 nanhu road, Jilin, Changchun, No. 6760 Co-patentee after: China National Gold Corporation Technology Center Patentee after: Changchun Gold Research Institute Co., Ltd. Address before: 130012 nanhu road, Jilin, Changchun, No. 6760 Co-patentee before: China National Gold Corporation Technology Center Patentee before: Changchun Gold Research Institute |