Production system for extracting germanium from germanium-containing material through oxygen pressure leaching

Abstract

The invention relates to the technical field of material production systems, in particular to a production system for extracting germanium from germanium-containing materials through oxygen pressure leaching, which comprises an oxygen pressure module, a separation module, an extraction module and a recovery module, the recycling module comprises a settling barrel, a rack, a driving mechanism, a rocker arm, a stirring mechanism and a pressing net; a plurality of liquid outlet pipes are arranged on the side wall of the precipitation barrel at intervals in the vertical direction, and all the liquid outlet pipes are provided with valves; the stirring mechanism is connected to the bottom end of the rocker arm and extends into the settling barrel; the driving mechanism is connected to the rack, and the driving mechanism is in driving connection with the rocker arm and enables the rocker arm to rotate around the axis in the vertical direction; the pressing net is slidably connected to the rocker arm in the vertical direction, a plurality of net holes are formed in the pressing net at intervals, a plurality of gravity balls are rotationally connected to the side wall of the pressing net in the circumferential direction, and all the gravity balls protrude out of the side wall of the pressing net. The recovery module is compact in design structure, can fully recover useful components in waste liquid, reduces resource waste, and improves production efficiency.

Description

Technical Field

[0001] The invention relates to the technical field of material production systems, and in particular to a production system for extracting germanium by oxygen pressure leaching of germanium-containing materials. Background Art

[0002] The extracted germanium is widely used in the fields of optical fiber communication, solar cells, chemical catalysts, infrared optics, aerospace, etc. With the continuous development of these fields, the demand for germanium is also increasing. After pretreatment (such as crushing, grinding, etc.), the germanium-containing materials enter the oxygen pressure leaching stage. Under the conditions of high pressure and oxygen, the materials come into contact with aqueous solutions or other liquids, and the germanium element is transferred to the liquid phase through chemical reactions. Subsequently, germanium is separated from the liquid phase by precipitation, extraction, ion exchange and other methods, and further enriched and purified. Finally, the waste liquid is recycled.

[0003] The application document with publication number CN104046801A discloses a method for extracting germanium from germanium silicon raw materials. The raw materials are tested and analyzed according to the traditional mineral component content detection method. When the germanium silicon raw materials contain silicon ≧2%, the raw materials are divided into compound raw materials and alloy raw materials, and the compound raw materials are leached by two-stage leaching, and the alloy raw materials are leached by three-stage leaching; each leaching stage uses at least two of fluoride, oxide and acid to prepare a leaching material, and the ratio of the leaching material to the raw material is 3-5, and the temperature is adjusted to 80-90°C, and the leaching is performed for 3-4h; the leaching residue is then placed in the next leaching material, and the previous leaching method is repeated; the solution is separated and extracted by a traditional separation and extraction method, so that ≧76% of silicon and ≧90% of germanium in the germanium silicon raw materials can be leached out.

[0004] In the prior art, waste liquid recovery mainly relies on manual operation, which reduces production efficiency. Summary of the invention

[0005] The purpose of the present invention is to improve production efficiency. In view of the above-mentioned shortcomings, a production system for extracting germanium by oxygen pressure leaching of germanium-containing materials is proposed.

[0006] The present invention adopts the following technical solution:

[0007] A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials, the system comprising an oxygen pressure module, a separation module, an extraction module and a recovery module; the oxygen pressure module reacts oxygen and germanium compounds to dissolve germanium in a leachate; the separation module separates the dissolved germanium from unreacted impurities by precipitation; the extraction module extracts germanium from the leachate to obtain extracted germanium and waste liquid; the recovery module recovers the waste liquid, the recovery module comprising a precipitation barrel, a frame, a driving mechanism, a rocker arm, a stirring mechanism and a pressing net; a plurality of liquid outlet pipes are spaced apart along the upper and lower directions on the side wall of the precipitation barrel, and all the liquid outlet pipes are provided with valves; the stirring mechanism is connected to the rocker arm at the bottom end, the stirring mechanism extends into the sedimentation barrel; the driving mechanism is connected to the frame, the driving mechanism drives the connected rocker arm, and causes the rocker arm to rotate around an axis in the up-down direction; the pressing net is slidably connected to the rocker arm in the up-down direction, a plurality of mesh holes are arranged at intervals on the pressing net, a plurality of gravity balls are circumferentially rotated on the side wall of the pressing net, all the gravity balls are arranged at intervals, all the gravity balls protrude from the side wall of the pressing net, the orthographic projection area of ​​the pressing net from top to bottom is smaller than the minimum area of ​​the cross-section of the barrel wall of the sedimentation barrel, before the driving mechanism drives the rocker arm, the pressing net is located above the sedimentation barrel, when the driving mechanism drives the rocker arm, the pressing net moves synchronously with the rocker arm, and the pressing net moves downward along the rocker arm under the action of gravity.

[0008] Optionally, the driving mechanism includes a driving member, a driving wheel and a driven wheel; the driving member is connected to the frame, the driving member is drivingly connected to a rotating rod, the rotating rod is rotatably connected to the frame, and the rotation axis of the rotating rod is arranged along the up and down directions; the driving wheel is connected to the rotating rod, and the rotation axis of the driving wheel coincides with the rotation axis of the rotating rod; the driven wheel is connected to the upper part of the rocker arm, and the driven wheel is meshed with the driving wheel; the rocker arm is connected to the rotating rod through a connecting member.

[0009] Optionally, the connecting member includes a connecting rod, a main ring and a secondary ring; the main ring and the secondary ring are respectively connected to two ends of the connecting rod, the main ring is connected to the outer side wall of the rotating rod; the secondary ring is sleeved on the outer side wall of the rocker arm.

[0010] Optionally, the connecting member further comprises a universal ball, which is connected to the rocker arm and is located between the secondary ring and the pressure net, and the universal ball is rotatably connected to the frame.

[0011] Optionally, the stirring mechanism includes a plurality of stirring rods, which are circumferentially connected to the bottom end of the rocker arm at intervals, the top ends of all the stirring rods are close to each other, the bottom ends are far away from each other, and all the stirring rods are bent.

[0012] Optionally, the stirring rod includes a connecting section, an inclined section and a stirring section; the connecting section is arranged in a horizontal direction, one end of the connecting section is connected to the bottom end of the rocker arm, and the other end is connected to one end of the inclined section, and the angle formed between the connecting section and the inclined section ranges from 100° to 170°; one end of the stirring section is connected to the other end of the inclined section, and the angle formed between the stirring section and the inclined section ranges from 80° to 120°.

[0013] Optionally, the side walls of all the stirring sections are connected with stirring blades, all the stirring blades extend toward a defense line away from the rocker arm, and the angle formed between the stirring blades and the stirring sections ranges from 80° to 120°.

[0014] The beneficial effects achieved by the present invention are:

[0015] 1. When the rocker arm rotates, the pressing net will also move downward synchronously. The pressing net can press the formed sediment to the bottom of the sedimentation barrel, which is helpful to separate the sediment;

[0016] 2. The recycling module has a compact design and can fully recycle the useful components in the waste liquid, reducing resource waste;

[0017] 3. Through the driving mechanism, rocker arm and other automated equipment, the automated operation of waste liquid recovery is realized, which improves production efficiency;

[0018] 4. Intelligent waste liquid recycling and processing reduces the complexity and errors of manual operations and improves production efficiency.

[0019] To further understand the features and technical contents of the present invention, please refer to the following detailed description and drawings of the present invention. However, the drawings provided are only for reference and description and are not intended to limit the present invention. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0021] Figure 2 It is a structural schematic diagram of the recovery module in the present invention;

[0022] Figure 3 This is a structural schematic diagram of the recycling module in the present invention from another angle;

[0023] Figure 4 It is a partial structural schematic diagram of the present invention;

[0024] Figure 5 It is a partial structural cross-sectional view of the present invention;

[0025] Figure 6 This is a schematic diagram of the overall structure of Embodiment 2 of the present invention;

[0026] Figure 7 Schematic diagram of the structure of the precipitation agent calculation module in the second embodiment of the present invention;

[0027] Figure 8 This is a relationship diagram between the actually measured humidity of the environment and the environmental humidity index in the second embodiment of the present invention.

[0028] Description of reference numerals:

[0029] 100. Sedimentation barrel;

[0030] 200, rack;

[0031] 300, stirring rod; 310, connecting section; 320, inclined section; 330, stirring section; 340, stirring blade;

[0032] 400, rocker arm;

[0033] 500, pressing net; 510, mesh; 520, gravity ball; 530, rotating ball;

[0034] 600, driving member; 610, driving wheel; 620, driven wheel; 630, rotating rod; 640, connecting rod; 650, main ring; 660, secondary ring; 670, universal ball. DETAILED DESCRIPTION

[0035] The following is an explanation of the embodiments of the present invention through specific embodiments. Those skilled in the art can understand the advantages and effects of the present invention from the contents disclosed in this specification. The present invention can be implemented or applied through other different specific embodiments, and the details in this specification can also be modified and changed in various ways based on different viewpoints and applications without departing from the spirit of the present invention. In addition, the drawings of the present invention are only simple schematic illustrations and are not depicted according to actual dimensions. It is stated in advance. The following embodiments will further explain the relevant technical contents of the present invention in detail, but the disclosed contents are not intended to limit the scope of protection of the present invention.

[0036] Embodiment 1: This embodiment provides a production system for extracting germanium by oxygen pressure leaching of germanium-containing materials, combined with Figures 1 to 5 shown.

[0037] A production system for extracting germanium from germanium-containing materials by oxygen pressure leaching, the system comprising an oxygen pressure module, a separation module, an extraction module and a recovery module; the oxygen pressure module reacts oxygen and germanium compounds to dissolve germanium in a leachate; the separation module separates the dissolved germanium from unreacted impurities by precipitation; the extraction module extracts germanium from the leachate to obtain extracted germanium and waste liquid; the recovery module recovers the waste liquid, the recovery module comprising a sedimentation barrel 100, a frame 200, a driving mechanism, a rocker arm 400, a stirring mechanism and a pressing net 500; a plurality of liquid outlet pipes are provided on the side wall of the sedimentation barrel 100 at intervals in the up and down directions, and all the liquid outlet pipes are provided with valves; the stirring mechanism is connected to the bottom end of the rocker arm 400, and the stirring mechanism extends into the sedimentation barrel 100; the driving mechanism is connected to the frame 200, and the driving mechanism drives the rocker arm 400, and The rocker arm 400 is rotated around an axis in the up-down direction; the pressing net 500 is connected to the rocker arm 400 by sliding in the up-down direction, and the motive force for the sliding in the up-down direction comes from the change in the position of the rocker arm, thereby generating a change in the friction between the pressing net and the pressing net and the gravity of the pressing net itself. The pressing net 500 is provided with a plurality of mesh holes 510 at intervals, and a plurality of gravity balls 520 are connected to the side wall of the pressing net 500 for circumferential rotation. All gravity balls 520 are arranged at intervals, and all gravity balls 520 protrude from the side wall of the pressing net 500. The orthographic projection area of ​​the pressing net 500 from top to bottom is smaller than the minimum area of ​​the cross section of the sedimentation barrel 100. Before the driving mechanism drives the rocker arm 400, the pressing net 500 is located above the sedimentation barrel 100. When the driving mechanism drives the rocker arm 400, the pressing net 500 moves synchronously with the rocker arm 400, and the pressing net 500 moves downward along the rocker arm 400 under the action of gravity.

[0038] Specifically, a plurality of rotating balls 530 are circumferentially arranged at the position where the pressing net 500 is rotatably connected to the rocker arm 400 . The plurality of rotating balls 530 are all rotatably connected to the pressing net 500 . The plurality of rotating balls 530 protrude from the pressing net 500 and abut against the outer side wall of the rocker arm 400 .

[0039] Two limit blocks are respectively provided on the side walls of the rocker arm 400 in the up and down directions, with a spacing between the two limit blocks. The upper limit block is made of rubber and can be deformed, while the lower limit block is made of metal with high hardness. Before the driving mechanism drives the rocker arm 400, the pressing net 500 is located above the upper limit block. When the driving mechanism drives the rocker arm 400, the pressing net 500 moves synchronously with the rocker arm 400, and the pressing net 500 is pressed against the upper limit block under the action of gravity to deform it. At this time, the pressing net 500 compresses the upper limit block and moves to the bottom of the upper limit block and moves downward along the rocker arm 400 until the pressing net 500 is against the top of the lower limit block. During the downward movement of the pressing net 500, pressure is applied to the newly formed floating sediment, thereby accelerating the downward movement of the sediment.

[0040] Optionally, the driving mechanism includes a driving member 600, a driving wheel 610 and a driven wheel 620; the driving member 600 is connected to the frame 200, and the driving member 600 is drivingly connected to a rotating rod 630, the rotating rod 630 is rotatably connected to the frame 200, and the rotation axis of the rotating rod 630 is arranged along the up and down directions; the driving wheel 610 is connected to the rotating rod 630, and the rotation axis of the driving wheel 610 coincides with the rotation axis of the rotating rod 630; the driven wheel 620 is connected to the upper part of the rocker arm 400, and the driven wheel 620 is meshed with the driving wheel 610; the rocker arm 400 is connected to the rotating rod 630 through a connecting member.

[0041] Specifically, the driving member 600 includes a driving motor and a driving gear set. The driving gear set is connected to the frame 200, and the driving motor is connected to the frame 200. The driving motor is connected to the rotating rod 630 through the driving gear set. When the driving motor works, it drives the driving gear set to rotate. The driving gear set drives the rotating rod 630. The rotation of the rotating rod 630 synchronously drives the driving wheel 610 to rotate.

[0042] Optionally, the connecting member includes a connecting rod 640, a main ring 650 and a secondary ring 660; the main ring 650 and the secondary ring 660 are respectively connected to the two ends of the connecting rod 640, the main ring 650 is connected to the outer wall of the rotating rod 630; the secondary ring 660 is sleeved on the outer wall of the rocker arm 400.

[0043] Optionally, the connecting member further includes a universal ball 670 , which is connected to the rocker arm 400 and located between the secondary ring 660 and the pressing net 500 , and the universal ball 670 is rotatably connected to the frame 200 .

[0044] Optionally, the stirring mechanism includes a plurality of stirring rods 300 , which are circumferentially connected to the bottom end of the rocker arm 400 at intervals, the top ends of all the stirring rods 300 are close to each other, the bottom ends are far away from each other, and all the stirring rods 300 are bent.

[0045] Optionally, the stirring rod 300 includes a connecting section 310, an inclined section 320 and a stirring section 330; the connecting section 310 is arranged in a horizontal direction, one end of the connecting section 310 is connected to the bottom end of the rocker arm 400, and the other end is connected to one end of the inclined section 320, and the angle formed between the connecting section 310 and the inclined section 320 ranges from 100° to 170°; one end of the stirring section 330 is connected to the other end of the inclined section 320, and the angle formed between the stirring section 330 and the inclined section 320 ranges from 80° to 120°.

[0046] Optionally, the side walls of all the stirring sections 330 are connected with stirring blades 340 , and all the stirring blades 340 extend toward a defense line away from the rocker arm 400 , and an angle formed between the stirring blades 340 and the stirring sections 330 ranges from 80° to 120°.

[0047] This embodiment solves the problem of lack of recycling steps in the traditional production system, and fully recovers the useful components in the waste liquid through the recycling module, thereby reducing the waste of resources.

[0048] Embodiment 2: This embodiment includes all the contents of embodiment 1, and provides a production system for extracting germanium by oxygen pressure leaching of germanium-containing materials, combined with Figures 6 to 8 shown.

[0049] A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials, the system also includes a precipitant calculation module and a communication module;

[0050] The precipitant calculation module is used to calculate the precipitant input amount and transmit the precipitant input amount to the communication module;

[0051] The communication module transmits the precipitant input amount to the user end.

[0052] Specifically, the precipitant calculation module and the recovery module are connected in communication. After the precipitant calculation module calculates the precipitant input amount, it can also be transmitted to the recovery module. The recovery module inputs the corresponding precipitant according to the corresponding value.

[0053] The precipitant calculation module includes an information storage submodule, a temperature detection submodule, a humidity detection submodule, a spectrometer and a control submodule;

[0054] The information storage submodule is used to store the waste liquid volume, the reaction molar ratio, the molar mass of the precipitant, the ideal value of the ambient temperature during spectroscopy detection, the ideal value of the ambient humidity during spectroscopy detection, the first selection threshold of the error index during spectroscopy detection, the second selection threshold of the error index during spectroscopy detection, the third selection threshold of the error index during spectroscopy detection, the ideal value of the stirring speed, the set value of the stirring speed, the ideal value of the stirring time and the set value of the stirring time, and transmit them to the control submodule;

[0055] The temperature detection submodule is used to detect and obtain the actual measured temperature of the environment and transmit it to the control submodule;

[0056] The humidity detection submodule is used to detect and obtain the actual humidity of the environment and transmit it to the control submodule;

[0057] The spectrometer is used to detect and obtain the actual concentration of heavy metals and transmit it to the control submodule;

[0058] The control submodule obtains an error index during spectral detection according to the ideal value of the ambient temperature corresponding to the formation of precipitation during spectral detection, the measured temperature of the environment, the ideal value of the stirring speed, the set value of the stirring speed, the ideal value of the stirring time and the set value of the stirring time; obtains a compensation percentage of the precipitant according to the error index during spectral detection, the first selection threshold value of the error index during spectral detection, the second selection threshold value of the error index during spectral detection and the third selection threshold value of the error index during spectral detection; obtains an ambient humidity index according to the measured humidity of the environment and the ideal value of the ambient humidity during spectral detection; obtains a heavy metal concentration index according to the measured concentration of the heavy metal, the measured temperature of the environment, the ideal value of the ambient temperature during spectral detection and the ambient humidity index; and obtains an amount of precipitant input according to the heavy metal concentration index, the waste liquid volume, the reaction molar ratio, the molar mass of the precipitant and the compensation percentage of the precipitant.

[0059] Optionally, when the control submodule calculates the amount of precipitant input, the following formula is satisfied:

[0060]

[0061]

[0062]

[0063]

[0064]

[0065] Among them, IA is the amount of precipitant input, HMC is the concentration index of heavy metals, V is the volume of waste liquid, R is the reaction molar ratio, MOP is the molar mass of the precipitant, and bf is the compensation percentage of the precipitant;

[0066] hmc is the measured concentration of heavy metals, temp t is the measured temperature of the environment, temp gpr is the ideal value of ambient temperature during spectral detection, and wet is the ambient humidity index;

[0067] sd t is the measured humidity of the environment, sd r It is the ideal value of ambient humidity for spectroscopy detection;

[0068] M is the error index during spectral detection, m1 is the first selection threshold of the error index during spectral detection, m2 is the second selection threshold of the error index during spectral detection, and m3 is the third selection threshold of the error index during spectral detection;

[0069] temp cdr is the ideal value of the ambient temperature corresponding to the formation of precipitation during spectroscopic detection, vr is the ideal value of stirring speed, v t is the setting value of stirring speed, t r is the ideal value of stirring time, t t It is the setting value of stirring time.

[0070] When controlling the submodule calculation, refer to the following code:

[0071]

[0072]

[0073]

[0074] The relationship diagram of the measured humidity of the reference environment and the environmental humidity index, where the dotted line represents the ideal value of the environmental humidity during spectral detection. The relationship diagram shows that the value of the environmental humidity index will only increase when the measured humidity of the environment exceeds the ideal value of the environmental humidity during spectral detection, which is used to reflect the potential impact of high humidity on the amount of precipitant input.

[0075] Specifically, the unit of the precipitant input is gram; the unit of the waste liquid volume is liter; the reaction molar ratio is determined according to the chemical reaction equation. For example, taking the precipitation of lead ions as an example, sodium hydroxide is used as the precipitant, and the reaction equation is as follows: 2+ +2NaOH→Pb(OH)2+2Na + From the reaction equation, we can see that 1 mole of Pb 2+ 2 moles of NaOH are required, i.e. the corresponding reaction molar ratio is 2; the molar mass of the precipitant is in grams per mole.

[0076] The unit of the measured concentration of heavy metals is milligrams per liter; the unit of the measured temperature of the environment is degrees Celsius; the unit of the ideal value of the ambient temperature during spectroscopy detection is degrees Celsius. The ideal value of the ambient temperature during spectroscopy detection refers to the appropriate ambient temperature suitable for the spectrometer to work, which can usually be queried in the relevant parameters set at the factory.

[0077] When calculating the concentration index of heavy metals, two influencing factors, temperature and humidity, are introduced. This is mainly because when the measured temperature of the environment is too high, the components inside the spectrometer will expand or deform due to heat, thereby affecting the stability of the optical path and the sensitivity of detection, which usually reduces the measured concentration of heavy metals. When the measured temperature of the environment is too low, the components inside the spectrometer will shrink, which will also affect the stability of the optical path and the sensitivity of detection, which usually reduces the measured concentration of heavy metals. When the measured humidity of the environment is too high, the components inside the spectrometer will become damp, affecting its performance, and causing scattering interference, reducing the intensity of the light signal, and thereby reducing the measured concentration of heavy metals. When the measured temperature of the environment is too low, the impact can be ignored.

[0078] The ideal value of ambient humidity during spectroscopy detection refers to the appropriate humidity for the spectrometer to work, which can usually be queried in the relevant parameters set at the factory.

[0079] The first selection threshold of the error index during spectroscopy detection, the second selection threshold of the error index during spectroscopy detection, and the third selection threshold of the error index during spectroscopy detection are set by those skilled in the art.

[0080] The unit of the ideal value of the ambient temperature corresponding to the formation of precipitation during spectral detection is degrees Celsius. When the measured temperature of the environment is too high or too low, it will lead to poor morphology of the precipitation or reduced purity, and a corresponding amount of precipitant needs to be added; the unit of the ideal value of the stirring speed and the set value of the stirring speed is revolutions per minute. The ideal value of the stirring speed is set by a technician in this field through table query. It is based on the evaluation of the corresponding waste liquid volume under an ideal stirring environment to obtain a specific value. However, due to environmental changes during stirring and the influence of stirring volatility, the technicians in this field will adjust some parameters before stirring, thereby obtaining the corresponding setting value of the stirring speed; the unit of the ideal value of the stirring time and the setting value of the stirring time is minutes, and the setting of the ideal value of the stirring time and the setting value of the stirring time is the same as the setting of the "ideal value of the stirring speed and the setting value of the stirring speed".

[0081] The above units are only examples, and those skilled in the art may set different units according to actual needs when implementing this solution.

[0082] This embodiment solves the problem of low rigor of the traditional production system. The precipitant calculation module can accurately calculate the required precipitant input amount according to production requirements, thereby ensuring the accuracy and efficiency of the precipitation process.

[0083] The contents disclosed above are only preferred feasible embodiments of the present invention, and do not limit the protection scope of the present invention. Therefore, all equivalent technical changes made using the contents of the present invention description and drawings are included in the protection scope of the present invention. In addition, the elements therein can be updated as technology develops.

Claims

1. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials, characterized in that: The system includes an oxygen pressure module, a separation module, an extraction module and a recovery module; The oxygen pressure module reacts oxygen with germanium compounds to dissolve germanium in the leaching solution; The separation module separates the dissolved germanium and unreacted impurities by precipitation; The extraction module extracts germanium from the leaching solution to obtain extracted germanium and waste liquid; The recovery module recovers the waste liquid, and the recovery module includes a sedimentation barrel, a frame, a driving mechanism, a rocker arm, a stirring mechanism and a pressing screen; The side wall of the sedimentation barrel is provided with a plurality of liquid outlet pipes spaced apart in the up-down direction, and all the liquid outlet pipes are provided with valves; The stirring mechanism is connected to the bottom end of the rocker arm, and the stirring mechanism extends into the sedimentation barrel; The driving mechanism is connected to the frame, and the driving mechanism drives the rocker arm to rotate around an axis in the up-down direction; The pressing net is connected to the rocker arm by sliding in the up-and-down directions, and a plurality of mesh holes are arranged at intervals on the pressing net. A plurality of gravity balls are connected to the side wall of the pressing net for circumferential rotation, and all the gravity balls are arranged at intervals, and all the gravity balls protrude from the side wall of the pressing net. The orthographic projection area of ​​the pressing net from top to bottom is smaller than the minimum area of ​​the cross-section of the wall of the sedimentation barrel. Before the driving mechanism drives the rocker arm, the pressing net is located above the sedimentation barrel. When the driving mechanism drives the rocker arm, the pressing net moves synchronously with the rocker arm, and the pressing net moves downward along the rocker arm under the action of gravity.

2. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 1, characterized in that: The driving mechanism comprises a driving member, a driving wheel and a driven wheel; The driving member is connected to the frame, the driving member is drivingly connected to a rotating rod, the rotating rod is rotatably connected to the frame, and the rotating axis of the rotating rod is arranged along the up-down direction; The driving wheel is connected to the rotating rod, and the rotation axis of the driving wheel coincides with the rotation axis of the rotating rod; The driven wheel is connected to the upper part of the rocker arm, and the driven wheel is meshed with the driving wheel; The rocker arm is connected to the rotating rod through a connecting piece.

3. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 2, characterized in that: The connecting member comprises a connecting rod, a main ring and a secondary ring; The main ring and the secondary ring are connected to the two ends of the connecting rod respectively, and the main ring is connected to the outer side wall of the rotating rod; The secondary ring is sleeved on the outer side wall of the rocker arm.

4. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 3, characterized in that: The connecting member also includes a universal ball, which is connected to the rocker arm and located between the auxiliary ring and the pressure net, and is rotatably connected to the frame.

5. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 4, characterized in that: The stirring mechanism comprises a plurality of stirring rods, which are connected to the bottom end of the rocker arm at intervals in a circumferential direction, the top ends of all the stirring rods are close to each other, the bottom ends are far away from each other, and all the stirring rods are bent.

6. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 5, characterized in that: The stirring rod comprises a connecting section, an inclined section and a stirring section; The connecting section is arranged in the horizontal direction, one end of the connecting section is connected to the bottom end of the rocker arm, and the other end is connected to one end of the inclined section, and the angle formed between the connecting section and the inclined section ranges from 100° to 170°; One end of the stirring section is connected to the other end of the inclined section, and the angle formed between the stirring section and the inclined section ranges from 80° to 120°.

7. A production system for extracting germanium by oxygen pressure leaching of germanium-containing materials as claimed in claim 6, characterized in that: The side walls of all the stirring sections are connected with stirring blades, and all the stirring blades extend toward a defense line away from the rocker arm, and the angle formed between the stirring blades and the stirring sections ranges from 80° to 120°.

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