CN211595753U - Device for removing zinc and iron in gold leaching barren solution of gold ore - Google Patents

Device for removing zinc and iron in gold leaching barren solution of gold ore Download PDF

Info

Publication number
CN211595753U
CN211595753U CN201922401989.8U CN201922401989U CN211595753U CN 211595753 U CN211595753 U CN 211595753U CN 201922401989 U CN201922401989 U CN 201922401989U CN 211595753 U CN211595753 U CN 211595753U
Authority
CN
China
Prior art keywords
iron
gold
zinc
buffer tank
thickener
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.)
Active
Application number
CN201922401989.8U
Other languages
Chinese (zh)
Inventor
李磊
袁欣波
翟永强
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.)
Shandong Zhongcheng Hongye Mining Technology Co ltd
Original Assignee
Shandong Zhongcheng Hongye Mining Technology 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 Shandong Zhongcheng Hongye Mining Technology Co ltd filed Critical Shandong Zhongcheng Hongye Mining Technology Co ltd
Priority to CN201922401989.8U priority Critical patent/CN211595753U/en
Application granted granted Critical
Publication of CN211595753U publication Critical patent/CN211595753U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model discloses a device and a method for removing zinc and iron in gold leaching barren solution of gold ores, which comprises a tube mixer for preliminary mixing raw materials, a buffer tank and a reaction kettle for chemical reaction, and is also provided with a thickener and a filter press for removing zinc and iron; the gold leaching barren liquor containing zinc and iron ions can be precipitated and filtered to remove zinc and iron ions and the like, so that the zinc and iron ions can be efficiently precipitated and separated. After separation, the supernatant can be continuously returned to the gold leaching system for use, so that better recycling is realized.

Description

Device for removing zinc and iron in gold leaching barren solution of gold ore
Technical Field
The utility model relates to a processing field of gold leaching barren liquor especially relates to a device that removes zinc iron in gold ore gold leaching barren liquor.
Background
The cyanidation method is a method of using a mixed solution composed of cyanide and the like as a solvent for leaching gold, and currently, a method of using a NaCN aqueous solution to leach gold in gold-containing ores and then extracting the gold from a gold-containing leaching solution is commonly used. The cyanidation method for extracting gold mainly includes cyanidation leaching, in the presence of oxygen or oxidant in cyanide solution with certain concentration, gold in gold-bearing ore reacts with cyanide to produce complex of gold and dissolves in the solution.
Since gold ores generally contain other metal elements, the cyanide tail solution often contains metal ions such as Zn2+, Fe2+, Pb2+, Cu2+, and the like, in addition to cyanides. For the recovery of metal ions, the traditional recovery mode cannot better separate and recover zinc and iron.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a remove device and method of zinc-iron in gold ore gold leaching barren liquor can deposit the gold leaching barren liquor that contains zinc-iron ion and filter and get rid of zinc-iron plasma, realizes the high-efficient sediment of zinc-iron ion, and separates. After separation, the supernatant can be continuously returned to the gold leaching system for use, so that better recycling is realized.
In order to solve the problems, the utility model discloses a device for removing zinc and iron in gold leaching barren solution of gold ores, which comprises a tube mixer for preliminary mixing raw materials, a buffer tank, a reaction kettle for chemical reaction, a thickener and a filter press for removing zinc and iron; the tube mixer is connected with the buffering feed inlet of the buffer tank, the buffering discharge port of the buffer tank is connected with the reaction feed inlet of the reaction kettle, the reaction discharge port is used for feeding the thickener, the upper layer of the thickener is provided with a clear water outlet, the bottom end of the thickener is provided with a precipitation discharge port, and the precipitation discharge port is connected with the filter press zinc iron mud.
Further, a buffer tank is arranged between the thickener and the filter press and used for temporarily storing zinc-iron mud sediment, and a pressure filter pump is arranged in the buffer tank and used for supplying materials to the filter press.
Further, the filter-pressing pump is provided with two pumps, wherein one pump is a working pump, and the other pump is a standby pump.
Further, an upper layer of paddle and a lower layer of paddle are arranged on the stirring shafts in the buffer tank, the reaction kettle and the buffer tank.
The beneficial effects of the utility model reside in that:
through the utility model discloses a device that removes zinc, iron in gold ore gold leaching barren solution can carry out effectual sediment and separation to the zinc iron ion in the gold ore gold leaching barren solution, and this reaction generates the cyanide coprecipitation of zinc and iron, and addition polyacrylamide flocculation, through the pressure filter solid-liquid separation after, the supernatant adds the alkaline back of sodium hydroxide and returns the gold leaching system and recycle.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. It is obvious that the drawings in the following description are some embodiments of the invention, and that for a person skilled in the art, other drawings can be derived from them without inventive effort.
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the drawings in the embodiments of the present invention are combined below to clearly and completely describe the technical solutions in the embodiments of the present invention. It is to be understood that the embodiments described are only some of the embodiments of the present invention, and not all of them. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The first embodiment is as follows:
the device for removing zinc and iron in the gold leaching barren solution of gold ore as shown in figure 1 comprises a tube mixer 1 for preliminary mixing raw materials, a buffer tank 2 and a reaction kettle 3 for chemical reaction, and is also provided with a thickener 4 and a filter press 5 for removing zinc and iron; wherein the pipe mixer links to each other with the buffering feed inlet 21 of buffer tank 2, and the reaction feed inlet 31 of reation kettle 3 is connected to the buffering discharge gate 22 of buffer tank, and reaction discharge gate 32 is the thickener feed, the thickener upper strata is equipped with clear water export 41, and the bottom is equipped with deposits discharge gate 42, deposit the discharge gate and connect pressure filter press filter zinc iron mud.
Wherein the thickener with still be equipped with buffer tank 6 between the pressure filter for the temporary storage that zinc iron mud deposits, buffer tank is equipped with filter-pressing pump 7, for the pressure filter feed.
The filter-pressing pump is provided with two pumps, wherein one pump is a working pump, and the other pump is a standby pump.
Wherein, the stirring shafts in the buffer tank, the reaction kettle and the buffer tank are respectively provided with an upper paddle layer and a lower paddle layer.
When in use, the device for removing zinc and iron in the gold leaching barren solution of the gold ore is used, and the device comprises the following steps:
(a) mixing raw material pipes: pre-mixing the zinc-iron-containing barren solution, sulfuric acid and a flocculating agent through a pipe mixer;
(b) mixing the buffer tank: inputting the premixed raw materials into a buffer tank, and stirring and mixing;
(c) and reaction in a reaction tank: inputting the mixed liquid into a reaction tank for full reaction and complexing to generate precipitate;
(d) and (3) thickening and separating: inputting the mixture obtained in the step into a thickener, separating the mixture by using the thickener, outputting supernatant liquor through a clear water outlet, and carrying out precipitation output through a precipitation discharge port;
(e) and filter pressing by a filter press: and (4) performing filter pressing precipitation by using a filter press to separate zinc-iron mud.
The above-mentioned embodiments are only intended to describe the preferred embodiments of the present invention, but not to limit the scope of the present invention, and various modifications and improvements made by those skilled in the art without departing from the spirit of the present invention should fall within the protection scope defined by the claims of the present invention.

Claims (4)

1. A device for removing zinc and iron in gold leaching barren solution of gold ore is characterized in that: comprises a tube mixer (1) for preliminary mixing raw materials, a buffer tank (2), a reaction kettle (3) for chemical reaction, a thickener (4) and a filter press (5) for removing zinc and iron; wherein the pipe mixer links to each other with buffering feed inlet (21) of buffer tank (2), and reaction feed inlet (31) of reation kettle (3) are connected in buffering discharge gate (22) of buffer tank, and reaction discharge gate (32) are the thickener feed, the thickener upper strata is equipped with clear water export (41), and the bottom is equipped with deposits discharge gate (42), deposit the discharge gate and connect pressure filter press zinc-iron mud.
2. The apparatus for removing zinc and iron in the gold leaching barren solution of gold ore according to claim 1, wherein: a buffer tank (6) is also arranged between the thickener and the filter press and used for temporarily storing the zinc iron mud precipitate, and the buffer tank is provided with a pressure filter pump (7) for feeding the filter press.
3. The apparatus for removing zinc and iron in the gold leaching barren solution of gold ore according to claim 2, characterized in that: the filter-pressing pump is equipped with two, and one of them is the working pump, and another is the standby pump.
4. The apparatus for removing zinc and iron in the gold ore leaching barren solution according to any one of claims 1 and 2, characterized in that: and upper and lower layers of blades are arranged on the stirring shafts in the buffer tank, the reaction kettle and the buffer tank.
CN201922401989.8U 2019-12-27 2019-12-27 Device for removing zinc and iron in gold leaching barren solution of gold ore Active CN211595753U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201922401989.8U CN211595753U (en) 2019-12-27 2019-12-27 Device for removing zinc and iron in gold leaching barren solution of gold ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201922401989.8U CN211595753U (en) 2019-12-27 2019-12-27 Device for removing zinc and iron in gold leaching barren solution of gold ore

Publications (1)

Publication Number Publication Date
CN211595753U true CN211595753U (en) 2020-09-29

Family

ID=72596563

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201922401989.8U Active CN211595753U (en) 2019-12-27 2019-12-27 Device for removing zinc and iron in gold leaching barren solution of gold ore

Country Status (1)

Country Link
CN (1) CN211595753U (en)

Similar Documents

Publication Publication Date Title
CN101838736B (en) Wet separation method for valuable metals in purified liquid cobalt slags of wet zinc smelting system
CN102010993B (en) Process for extracting nickel and cobalt from laterite by ore pulp extraction technology
CN104475261A (en) Method for recovering low-grade copper-zinc mineral from cyanidation tailings
CN102206759A (en) Decyanation method and apparatus of cyanogen-containing tailings
CN100371471C (en) New treating method for nickel oxide ore
CN107034359A (en) A kind of utilization cyanide wastewater reclaims the method for neutralizing valuable metal in waste residue
CN102899499B (en) Process and device for recovering noble metals of zinc smelting acid leaching residues
CN101935754A (en) Method for treating lead-containing high electrum concentrate
CN103320624B (en) Method for selectively extracting gold and silver from copper anode slime
CN107298458A (en) A kind of utilization acid solution is with extractant to separate the retracting device of neodymium iron boron waste material middle rare earth
CN108866337B (en) A method of processing metal sludge
CN103276221A (en) Method for recovering copper from copper flotation system liquids of tailings after cyaniding gold extraction
CN211595753U (en) Device for removing zinc and iron in gold leaching barren solution of gold ore
CN211079293U (en) Nickel hydroxide cobalt sediment leaches device
CN103966433A (en) Method for extracting copper, gold and silver from copper oxide ore
CN206570378U (en) Production line for oxygen pressure leaching of uranium and molybdenum from uranium and molybdenum ore
CN107746965B (en) A kind of method of germanium vacuum distillation slag recovery indium germanium
CN104561563A (en) Indium-rich slag reduction presoaking technology and device thereof
CN102908970B (en) Two-way Cycle injection reactor
CN105177283A (en) Deep leaching method of copper-containing alloy leaching tailings
CN103738928A (en) Method for recycling selenium in electrolytic manganese anode slime through ultrasonic enhancement
CN111101000A (en) Device and method for removing zinc and iron in gold leaching barren solution of gold ore
CN108342574B (en) Countercurrent washing device for rare earth precipitation and method for recycling rare earth oxalic acid precipitation mother liquor and washing liquor by using countercurrent washing device
CN110550664B (en) Method for preparing iron oxide red by roasting cyanide tailings containing arsenic
CN217324228U (en) Aerify and return thick liquid device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant