CN205501382U - Recovery system is depositd in oxidation liquid aurin ore deposit - Google Patents

Recovery system is depositd in oxidation liquid aurin ore deposit Download PDF

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Publication number
CN205501382U
CN205501382U CN201620307343.7U CN201620307343U CN205501382U CN 205501382 U CN205501382 U CN 205501382U CN 201620307343 U CN201620307343 U CN 201620307343U CN 205501382 U CN205501382 U CN 205501382U
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China
Prior art keywords
sedimentation tank
efficient sedimentation
oxidation solution
pipeline
oxidation liquid
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CN201620307343.7U
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Chinese (zh)
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许立中
顾恒心
张�林
顾继彬
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Liaoning Huibao Gold Industry Co Ltd
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Liaoning Huibao Gold Industry Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model belongs to the technical field of the mineral resources ore dressing and specifically relates to a recovery system is depositd in oxidation liquid aurin ore deposit, including buffering sedimentation tank, neutralizing tank and a plurality of high -efficient sedimentation tank, wherein a plurality of high -efficient sedimentation tanks pass through overflow passage establishes ties in proper order, and a high -efficient sedimentation tank of oxidation liquid input pipeline and outer end communicates with each other, keeps away from the high -efficient sedimentation tank of oxidation liquid input pipeline one end then through the pipeline with the buffering sedimentation tank communicates with each other, the buffering sedimentation tank pass through the pipeline with the neutralizing tank communicates with each other the buffering sedimentation tank with be equipped with the pump on the communicating pipeline of neutralizing tank. The utility model discloses an increase the precipitation time of a plurality of high -efficient sedimentation tanks extension oxidation liquid to aurin ore deposit in the assurance oxidation liquid is fully depositd, and it is fast also effectively to slow down the oxidation liquid stream, avoiding, sedimentary aurin ore deposit suspends again.

Description

Oxidation solution Gold Concentrate under Normal Pressure precipitation recovery system
Technical field
This utility model relates to mineral resources ore dressing field, specifically a kind of oxidation solution aurin Ore deposit precipitation recovery system.
Background technology
Gold Concentrate under Normal Pressure recovery process flow process of the prior art is as follows: Gold Concentrate under Normal Pressure through one-level, two grades Pool together after biological oxidation, and after the backwash step by step of three concentrators, the biggest portion Parting concentrate flows to cyaniding workshop and carries out cyaniding, and liquid (the i.e. oxygen produced in backwash process Change liquid) need to be flowed to by the overflow passage of every concentrator the buffer-precipitation pond of neutralization department is entered Row buffering precipitates, and its objective is that the Gold Concentrate under Normal Pressure making to suspend in oxidation solution precipitates, reduces and run off, Improve the response rate of gold.As it is shown in figure 1, the oxidation solution Gold Concentrate under Normal Pressure precipitation in existing technological process Recovery system mainly includes a buffer-precipitation pond and a neutralization chamber, and oxidation solution flows directly into slow Rush in sedimentation tank, then flowed in neutralization chamber by pumping action, then in neutralization chamber, add white lime enter Row neutralizes, and the mine tailing finally produced is reclaimed, but finds in actual production is put into practice, this Although precipitation recovery system has certain precipitation, but effect is not highly desirable, still has one Quantitative Gold Concentrate under Normal Pressure runs off, and finds, why can produce this after repeatedly observing and testing Situation, the oxidation liquid measure produced mainly due to every day is bigger, thus results in inflow buffering heavy The oxidation solution flow velocity in fall pond is relatively big, and impulsive force is relatively strong, so, not only makes oxidation solution not foot Enough sedimentation times, and the Gold Concentrate under Normal Pressure settled suspends under the impact of oxidation solution flow velocity Getting up, thus cause loss, the oxidation solution Gold Concentrate under Normal Pressure precipitation in the most existing technological process reclaims System needs to make improvements.
Utility model content
The purpose of this utility model is to provide a kind of oxidation solution Gold Concentrate under Normal Pressure precipitation recovery system, logical Spend the sedimentation time increasing multiple efficient sedimentation tank prolongation oxidation solution, thus ensure in oxidation solution Gold Concentrate under Normal Pressure fully precipitates, and the most effectively slows down oxidation solution flow velocity, it is to avoid the most deposited aurin Ore deposit Eddy diffusion.
The purpose of this utility model is achieved through the following technical solutions:
A kind of oxidation solution Gold Concentrate under Normal Pressure precipitation recovery system, including buffer-precipitation pond, neutralization chamber and many Individual efficient sedimentation tank, wherein said multiple efficient sedimentation tank are sequentially connected in series by overflow passage, oxygen Change liquid intake line to communicate with an efficient sedimentation tank of outermost end, the efficient sedimentation tank of the other end Then being communicated with described buffer-precipitation pond by pipeline, pipeline is passed through with described in described buffer-precipitation pond Neutralization chamber communicates, and is provided with pump on the pipeline that described buffer-precipitation pond communicates with described neutralization chamber.
The quantity of described efficient sedimentation tank is two.
Described efficient sedimentation tank is rustless steel efficient sedimentation tank.
Described oxidation solution intake line is gravity line.
Efficient sedimentation tank and described buffer-precipitation pond away from described oxidation solution intake line one end The pipeline being connected is gravity line.
Advantage of the present utility model with good effect is:
1, this utility model extends the sedimentation time of oxidation solution by increasing multiple efficient sedimentation tank, Thus ensure that the Gold Concentrate under Normal Pressure in oxidation solution fully precipitates, and the most effectively slow down oxidation solution flow velocity, Avoid the most deposited Gold Concentrate under Normal Pressure Eddy diffusion.
2, this utility model simple in construction, but considerably increase economic benefit, before not improving, A buffer-precipitation pond be need to quarterly clear up, Gold Concentrate under Normal Pressure 12 tons, ton grade cleared out the most every time Average out to 60g, after technological improvement, No. 1 efficient sedimentation tank 5 of each two moon cleaning, flat The most clear Gold Concentrate under Normal Pressure 20 tons that obtains, ton grade average out to 60g, clears up one time 2 for every four months Number efficient sedimentation tank, the most clear the Gold Concentrate under Normal Pressure 16 tons, ton grade average out to 30g, increase Add benefit obvious.
Accompanying drawing explanation
Fig. 1 is that oxidation solution Gold Concentrate under Normal Pressure of the prior art precipitates recovery system schematic diagram,
Fig. 2 is schematic diagram of the present utility model.
Wherein, 1 is oxidation solution intake line, and 2 is buffer-precipitation pond, and 3 is pump, and 4 for neutralizing Groove, 5 is efficient sedimentation tank.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
As in figure 2 it is shown, this utility model includes buffer-precipitation pond 2, neutralization chamber 4 and multiple high Effect sedimentation tank 5, wherein said multiple efficient sedimentation tank 5 are sequentially connected in series by pipeline, oxidation solution Intake line 1 communicates with an efficient sedimentation tank 5 of outermost end, the efficient sedimentation tank of the other end 5 are communicated with described buffer-precipitation pond 2 by pipeline, and pipeline is passed through in described buffer-precipitation pond 2 Communicate with described neutralization chamber 4, at the pipe that described buffer-precipitation pond 2 communicates with described neutralization chamber 4 Road is provided with pump 3.In the present embodiment, described efficient sedimentation tank 5 is rustless steel efficient sedimentation tank, The manufacturer of the rustless steel efficient sedimentation tank employed in the present embodiment is Dandong Solenognathus chemical fibre Machinery Co., Ltd., is provided with two efficient sedimentation tank 5 altogether in the present embodiment.
The plurality of efficient sedimentation tank 5 passes sequentially through overflow passage series connection, is i.e. full of when oxidation solution After one efficient sedimentation tank 5, it is next the most heavy that the oxidation solution of spilling is flowed into by overflow passage In pond, shallow lake 5, described oxidation solution intake line 1 and away from described oxidation solution intake line 1 one The pipeline that the efficient sedimentation tank 5 of end is connected with described buffer-precipitation pond 2 is gravity line, institute Stating gravity line and the most do not apply pressure, rely solely on fluid reforms Bottomhole pressure, institute certainly State the oxidation solution in buffer-precipitation pond 2 then to be flowed in neutralization chamber 4 by pump 3 effect.
Operation principle of the present utility model is:
As it is shown in figure 1, Gold Concentrate under Normal Pressure precipitation recovery system master in oxidation solution in existing technological process Including a buffer-precipitation pond 2 and a neutralization chamber 4, as in figure 2 it is shown, this utility model Oxidation solution input side in described buffer-precipitation pond 2 adds multiple efficient sedimentation tank 5, significantly Improve gold recovery.
Former process condition:
Quarterly buffer-precipitation pond 2 of cleaning, clears out Gold Concentrate under Normal Pressure 12 tons, ton the most every time Grade average out to 60g.
Situation after technological improvement:
No. 1 efficient sedimentation tank 5 of each two moon cleaning, the most clear the Gold Concentrate under Normal Pressure 20 Ton, ton grade average out to 60g, No. 2 efficient sedimentation tank of cleaning in every four months, the most often The secondary clear Gold Concentrate under Normal Pressure 16 tons that obtains, ton grade average out to 30g, increase benefit obvious.

Claims (5)

1. an oxidation solution Gold Concentrate under Normal Pressure precipitation recovery system, it is characterised in that: include that buffering is heavy Pond, shallow lake (2), neutralization chamber (4) and multiple efficient sedimentation tank (5), wherein said multiple efficiently Sedimentation tank (5) is sequentially connected in series by overflow passage, oxidation solution intake line (1) and outermost end An efficient sedimentation tank (5) communicate, the efficient sedimentation tank (5) of the other end then passes through pipeline Communicating with described buffer-precipitation pond (2), described buffer-precipitation pond (2) passes through pipeline with described Neutralization chamber (4) communicates, and communicates with described neutralization chamber (4) described buffer-precipitation pond (2) Pipeline be provided with pump (3).
Oxidation solution Gold Concentrate under Normal Pressure the most according to claim 1 precipitation recovery system, its feature It is: the quantity of described efficient sedimentation tank (5) is two.
Oxidation solution Gold Concentrate under Normal Pressure the most according to claim 1 and 2 precipitation recovery system, its It is characterised by: described efficient sedimentation tank (5) is rustless steel efficient sedimentation tank.
Oxidation solution Gold Concentrate under Normal Pressure the most according to claim 1 precipitation recovery system, its feature It is: described oxidation solution intake line (1) is gravity line.
Oxidation solution Gold Concentrate under Normal Pressure the most according to claim 1 precipitation recovery system, its feature It is: away from the efficient sedimentation tank (5) of described oxidation solution intake line (1) one end with described The pipeline that buffer-precipitation pond (2) is connected is gravity line.
CN201620307343.7U 2016-04-13 2016-04-13 Recovery system is depositd in oxidation liquid aurin ore deposit Active CN205501382U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620307343.7U CN205501382U (en) 2016-04-13 2016-04-13 Recovery system is depositd in oxidation liquid aurin ore deposit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620307343.7U CN205501382U (en) 2016-04-13 2016-04-13 Recovery system is depositd in oxidation liquid aurin ore deposit

Publications (1)

Publication Number Publication Date
CN205501382U true CN205501382U (en) 2016-08-24

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Country Status (1)

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CN (1) CN205501382U (en)

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