Lunar soil oxygen production reactor system

By using solar heating and hourglass or spiral tube structures in the monthly soil oxygen reactor system, the continuity and low energy consumption production of moon soil oxygen -based oxygen -made oxygen is realized, and the high energy consumption in existing technology is high and the power consumption is high and the power consumption is high The problem of low oxygen -making efficiency.

CN119346053APending Publication Date: 2025-01-24CHINA ACADEMY OF SPACE TECHNOLOGY
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Patent Information

Application Number
CN202411109419.0
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-08-13
Publication Date
2025-01-24

AI Technical Summary

Technical Problem

The existing lunar soil oxygen-making reactor system has problems such as high power consumption, low oxygen-making efficiency, and difficulty in continuous production.

Method used

A lunar soil oxygen production reactor system is designed, which uses solar energy as the main energy source. The solar energy is converted into heat energy of the heat transfer medium through a heat absorber. It is combined with an hourglass-shaped or spiral tube structure of the reaction chamber to realize the production of lunar soil raw materials. Continuous supply and continuous discharge of slag materials, and the use of single-chip microcomputer controller to accurately control the reaction process.

Benefits of technology

It achieves continuous and low-energy production of lunar soil oxygen production, reduces power consumption, and improves oxygen production efficiency. It is suitable for various methods such as hydrogen reduction, methane reduction, and fluorinated lunar soil oxygen production.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention provides a lunar soil oxygen production reactor system. The lunar soil oxygen production reactor system comprises a reaction chamber subsystem, a heat supply subsystem, a material supply and slag discharge subsystem, a gas supply and exhaust subsystem and a control subsystem, the reaction chamber subsystem is used for providing a lunar soil oxygen generation reaction place; the material supply and slag discharge subsystem is used for continuously supplying lunar soil raw materials and discharging slag materials for the lunar soil oxygen production reactor system; the gas supply and exhaust subsystem is used for continuously supplying reaction gas and exhausting product gas to the lunar soil oxygen production reactor system; the heat supply subsystem is used for converting sunlight energy into heat energy of a heat transfer working medium through a heat absorber and supplying heat energy to the lunar soil oxygen production reactor system; and the control subsystem is used for controlling heat energy supply, lunar soil raw material supply, slag discharge and gas supply and discharge of the lunar soil oxygen production reactor system. The invention has the characteristics of high oxygen production efficiency, low energy consumption and continuous production.
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Description

Technical Field

[0001] The present invention relates to the technical field of space resource development and utilization, and in particular to a lunar soil oxygen production reactor system. Background Art

[0003] The trend of future manned deep space exploration is to realize long-term and sustainable exploration activities of human beings on extraterrestrial bodies. This requires human beings to have the ability to develop and utilize space resources. Therefore, the development and utilization of space resources has become an important development direction in the current aerospace field. Among them, lunar soil oxygen production technology is an important technology in the field of space resource development and utilization.

[0004] The lunar surface is covered with a large amount of lunar soil, which has an oxygen content of about 40%, a thickness of about 4 to 15 meters, and a median particle size of about 40 to 130 um. The lunar soil contains about 15% ilmenite, and its chemical formula is FeO·TiO2. The lunar soil ilmenite particles can produce oxygen in situ on the lunar surface through hydrogen reduction. The technologies and methods for producing oxygen using lunar soil mainly include: hydrogen reduction method, methane reduction method, fluorination method and molten salt electrolysis method. In addition to the molten salt electrolysis method, the other three methods of producing oxygen from lunar soil all require the use of a high-temperature reactor to provide a reaction site for the lunar soil and the reaction gas. Therefore, the lunar soil oxygen production reactor system is the most important part of the lunar soil oxygen production technology.

[0005] However, in the existing technology, the lunar soil oxygen production reactor system generally has problems such as high power consumption, low oxygen production efficiency, and difficulty in continuous production. Summary of the invention

[0006] In order to solve the technical problems existing in the above-mentioned prior art, the purpose of the present invention is to provide a lunar soil oxygen production reactor system, which has the characteristics of high oxygen production efficiency, low energy consumption and continuous production.

[0007] In order to achieve the above-mentioned invention object, the present invention provides a lunar soil oxygen production reactor system, including: a reaction chamber subsystem, a heating subsystem, a material supply and slag discharge subsystem, a gas supply and exhaust subsystem and a control subsystem;

[0008] The reaction chamber subsystem is used to provide a place for the lunar soil to produce oxygen;

[0009] The feeding and slag discharge subsystem includes a feeding bin and a slag bin, both of which are connected to the reaction chamber cavity of the reaction chamber subsystem to continuously supply lunar soil raw materials and discharge slag materials to the lunar soil oxygen production reactor system;

[0010] The gas supply and exhaust subsystem is used to continuously supply reaction gas and exhaust product gas to the lunar soil oxygen production reactor system;

[0011] The heating subsystem converts sunlight energy into thermal energy of a heat transfer medium through a heat absorber, thereby supplying thermal energy to the lunar soil oxygen production reactor system.

[0012] According to a technical solution of the present invention, the reaction chamber subsystem further includes a reaction chamber shell, the reaction chamber inner cavity is arranged in the reaction chamber shell, and a working medium cavity for filling the heat transfer working medium is provided between the reaction chamber shell and the reaction chamber inner cavity;

[0013] The inner cavity of the reaction chamber is a plurality of interconnected hourglass-shaped reaction chambers, or

[0014] The inner cavity of the reaction chamber is a plurality of interconnected spiral tubes.

[0015] The arrangement of the multiple hourglass-shaped reaction chambers or the multiple spiral tubes is coaxial arrangement and / or parallel axis arrangement.

[0016] According to a technical solution of the present invention, the heating subsystem further includes a heat pipe, a circulation pump and a reflector, and the heat pipe connects the circulation pump, the heat absorber and the working medium chamber to form a loop.

[0017] According to a technical solution of the present invention, the feed bin is arranged directly above the inner cavity of the reaction chamber and is connected to the inner cavity of the reaction chamber, and the lunar soil raw material is continuously supplied to the inner cavity of the reaction chamber by gravity;

[0018] The slag bin is arranged directly below the inner cavity of the reaction chamber and is communicated with the inner cavity of the reaction chamber, and the slag is continuously discharged by gravity.

[0019] According to a technical solution of the present invention, a feed valve and a discharge valve are respectively provided on the inlet end and the outlet end of the feed bin;

[0020] The inlet end and the outlet end of the slag bin are provided with a slag inlet valve and a slag outlet valve.

[0021] According to a technical solution of the present invention, the air supply and exhaust subsystem includes an air intake valve, an exhaust valve and an air delivery pipe;

[0022] The air inlet valve is arranged at the lower part of the reaction chamber subsystem, and the air exhaust valve is arranged at the upper part of the reaction chamber subsystem.

[0023] According to a technical solution of the present invention, the control subsystem is used to control the heat energy supply, lunar soil raw material supply and slag discharge, and gas supply and discharge of the lunar soil oxygen production reactor system;

[0024] The control subsystem includes a single-chip microcomputer controller, a thermocouple, a gas pressure gauge and a piezoelectric sensor, and the air intake valve, the exhaust valve, the feed valve, the discharge valve, the slag inlet valve and the slag discharge valve are electrically connected to the single-chip microcomputer controller;

[0025] The thermocouple, the gas pressure gauge and the piezoelectric sensor are all electrically connected to the single chip controller.

[0026] According to a technical solution of the present invention, the heating subsystem is further configured with a director, and the director is controlled by the single-chip controller to point to the sun, so as to reflect and focus the sunlight on the heat absorber.

[0027] According to a technical solution of the present invention, the feed valve, the discharge valve, the slag feed valve and the slag discharge valve are all equipped with servo motors, and any of the servo motors is electrically connected to the single-chip controller.

[0028] According to a technical solution of the present invention, a heat insulating layer is provided on the outer surface of the reaction chamber shell.

[0029] Compared with the prior art, the present invention has the following beneficial effects:

[0030] The present invention proposes a lunar soil oxygen production reactor system, which adopts solar energy as the main energy source, converts solar energy into thermal energy of a heat transfer medium through a heat absorber, and continuously supplies lunar soil raw materials and discharges slag to the lunar soil oxygen production reactor system through a feeding and slag discharge subsystem, thereby realizing continuous and low-energy production of lunar soil oxygen, thereby effectively reducing the power consumption of the lunar soil oxygen production system. At the same time, it is also beneficial to the further utilization of the slag after the reaction, which is beneficial to people's large-scale oxygen production activities and production of rocket propellants on the lunar surface in the future, and laying a foundation for people to carry out comprehensive utilization of lunar resources on the lunar surface.

[0031] The present invention utilizes a reflector to reflect and converge sunlight onto a heat absorber, and efficiently converts solar energy into thermal energy, thereby reducing dependence on external energy consumption and lowering energy consumption. The design of the feeding unit and the slag discharge unit of the feeding and slag discharge subsystem allows for continuous supply of lunar soil raw materials and continuous discharge of slag materials. A feeding valve and a discharging valve are respectively provided on the inlet and outlet ends of the feeding bin, and a slag feeding valve and a slag discharging valve are provided on the inlet and outlet ends of the slag bin. By controlling the opening and closing of the valves in sequence, the pressure in the inner cavity of the reaction chamber can be kept stable, and the continuity of oxygen production can be achieved. The single-chip microcomputer controller is used to accurately control the air intake valve, the exhaust valve, the feed valve, etc., and the corresponding valves can be adjusted according to the air pressure and temperature in the inner cavity of the reaction chamber to achieve automatic and precise control of the oxygen production reaction, thereby achieving continuous production of lunar soil oxygen production, improving the reaction efficiency of lunar soil oxygen production, and being beneficial to improving the oxygen production yield of the system and achieving large-scale oxygen production.

[0032] The lunar soil oxygen production reactor system proposed in the present invention can not only be used for hydrogen reduction of lunar soil to produce oxygen, but can also be applied to methane reduction of lunar soil to produce oxygen and fluorination of lunar soil to produce oxygen.

[0033] The lunar soil oxygen production reactor system proposed in the present invention can not only be used to produce oxygen from the lunar soil, but can also be used to heat the lunar soil to collect helium-3 gas, heat frozen soil or water ice to collect water vapor, etc., and has broad application prospects. BRIEF DESCRIPTION OF THE DRAWINGS

[0034] In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments are briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention, and for ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work.

[0035] Figure 1 A composition diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention;

[0036] Figure 2 It is a schematic structural diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention;

[0037] Figure 3 This is a working principle diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention;

[0038] Figure 4 An energy flow diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention;

[0039] Figure 5 A lunar soil flow path diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention;

[0040] Figure 6 This is a gas flow diagram of a lunar soil oxygen production reactor system in one embodiment of the present invention.

[0041] The corresponding relationship between the reference numerals and component names is as follows:

[0042] 1. Reaction chamber subsystem; 2. Heating subsystem; 3. Feeding and slag removal subsystem; 4. Gas supply and exhaust subsystem; 5. Control subsystem;

[0043] 11. Reaction chamber shell; 12. Reaction chamber inner cavity; 13. Heat insulation layer; 14. Bracket;

[0044] 21. Orienter; 22. Reflector; 23. Heat absorber; 24. Heat pipe; 25. Heat transfer medium; 26. Circulation pump;

[0045] 31. Feed bin; 32. Feed valve; 33. Discharge valve; 34. Slag bin; 35. Slag feed valve; 36. Slag discharge valve;

[0046] 41. Intake valve; 42. Exhaust valve; 43. Gas pipe;

[0047] 51. Gas pressure gauge; 52. Thermocouple; 53. Piezoelectric sensor; 54. Single chip controller; 55. Servo motor. DETAILED DESCRIPTION

[0048] The description of the embodiments of this specification should be combined with the corresponding drawings, which should be considered as part of the complete specification. In the drawings, the shape or thickness of the embodiments may be enlarged and indicated for simplification or convenience. Furthermore, the parts of each structure in the drawings will be described separately. It is worth noting that the elements not shown in the drawings or not described in words are in a form known to ordinary technicians in the relevant technical field.

[0049] The description of the embodiments herein and any reference to directions and orientations are only for the convenience of description and are not to be construed as any limitation on the scope of protection of the present invention. The following description of the preferred embodiments may involve combinations of features, which may exist independently or in combination, and the present invention is not particularly limited to the preferred embodiments. The scope of the present invention is defined by the claims.

[0050] Example 1

[0051] like Figures 1 to 6 As shown, a lunar soil oxygen production reactor system provided by the present invention includes a reaction chamber subsystem 1, a heating subsystem 2, a material feeding and slag removal subsystem 3, a gas supply and exhaust subsystem 4 and a control subsystem 5.

[0052] The reaction chamber subsystem 1 provides the system with a place for the lunar soil oxygen production reaction. The reaction chamber subsystem 1 includes a reaction chamber shell 11 and a reaction chamber inner cavity 12. The reaction chamber inner cavity 12 is arranged in the reaction chamber shell 11. Between the reaction chamber shell 11 and the reaction chamber inner cavity 12 is a working medium cavity for filling the heat transfer medium 25. That is, the heat transfer medium 25 is heated in the working medium cavity to provide heat energy for the reaction chamber inner cavity 12.

[0053] The heating subsystem 2 supplies heat energy to the system. The heating subsystem 2 converts the sunlight energy into the heat energy of the heat transfer medium 25 through the heat absorber 23, and supplies heat energy to the lunar soil oxygen production reactor system. The heating subsystem 2 also includes a heat pipe 24, a circulation pump 26 and a reflector 22. The heat pipe 24 connects the circulation pump 26, the heat absorber 23 and the working medium chamber to form a loop.

[0054] The feeding and slag discharge subsystem 3 includes a feeding bin 31 and a slag bin 34, both of which are connected to the inner chamber 12 of the reaction chamber subsystem 1, and continuously supply lunar soil raw materials and discharge slag materials to the lunar soil oxygen production reactor system; the feeding bin 31 is arranged directly above the inner chamber 12 of the reaction chamber, and is connected to the inner chamber 12 of the reaction chamber, and continuously supplies lunar soil raw materials to the inner chamber 12 of the reaction chamber by gravity; the slag bin 34 is arranged directly below the inner chamber 12 of the reaction chamber, and is connected to the inner chamber 12 of the reaction chamber, and continuously discharges slag materials by gravity. A feeding valve 32 and a discharging valve 33 are respectively provided at the inlet and outlet ends of the feeding bin 31; a slag feeding valve 35 and a slag discharging valve 36 are provided at the inlet and outlet ends of the slag bin 34.

[0055] The gas supply and exhaust subsystem 4 is used to continuously supply reaction gas and exhaust product gas to the lunar soil oxygen production reactor system. The gas supply and exhaust subsystem 4 includes an intake valve 41, an exhaust valve 42 and a gas pipeline 43. The intake valve 41 is arranged at the lower part of the reaction chamber subsystem 1, and the exhaust valve 42 is arranged at the upper part of the reaction chamber subsystem 1, that is, the reaction gas flows from bottom to top in the reaction chamber inner cavity 12 by the pressure difference.

[0056] The control subsystem 5 is used to control the heat energy supply, lunar soil raw material supply and slag material discharge, and gas supply and discharge of the lunar soil oxygen production reactor system. The control subsystem 5 includes a single-chip microcomputer controller 54, a thermocouple 52, a gas pressure gauge 51, and a piezoelectric sensor 53. The air inlet valve 41, the exhaust valve 42, the feed valve 32, the discharge valve 33, the slag inlet valve 35, and the slag discharge valve 36 are electrically connected to the single-chip microcomputer controller 54. The thermocouple 52, the gas pressure gauge 51, and the piezoelectric sensor 53 are all electrically connected to the single-chip microcomputer controller 54.

[0057] The heating subsystem 2 is also equipped with a director 21 , which is controlled by a single-chip controller 54 to point to the sun, and reflects and converges sunlight onto the heat absorber 23 .

[0058] The feed valve 32, the discharge valve 33, the slag feed valve 35 and the slag discharge valve 36 are all equipped with a servo motor 55, and any servo motor 55 is electrically connected to the single-chip controller 54, so as to realize automatic control of the feed valve 32, the discharge valve 33, the slag feed valve 35 and the slag discharge valve 36. It can be understood that any part involving switches in the lunar soil oxygen production reactor system of the present invention can be automatically controlled by the single-chip controller 54.

[0059] A heat insulating layer 13 is provided on the outer surface of the reaction chamber shell 11. A support 14 is also provided on the reaction chamber shell 11.

[0060] like Figure 2As shown, the inner cavity 12 of the reaction chamber is a plurality of interconnected hourglass-shaped reaction chambers, which adopt a conical structure or a hemispherical structure, the number of which is 1 to 100 pairs, and the volume of the inner cavity 12 of the reaction chamber in the shell 11 of the reaction chamber is 10 to 90%, and the arrangement of the conical structure or the hemispherical structure is coaxial arrangement and / or parallel axis arrangement. The lunar soil raw material flows downward from the feed bin 31 at the top of the reaction chamber through the inner cavity 12 of the reaction chamber, reacts with the reaction gas in the inner cavity 12 of the reaction chamber, and then is converted into slag and flows into the slag bin 34 at the bottom of the reaction chamber 1.

[0061] In addition, the hourglass-shaped reaction chamber can also adopt other polyhedral cones, such as triangular pyramids, quadrangular pyramids, etc. Of course, other structures that can delay or slowly discharge materials can also be used.

[0062] like Figure 4 As shown, Figure 4 The schematic diagram of the energy flow path of the present invention. The present invention uses solar thermal conversion technology to convert solar energy into thermal energy. First, the reflector 22 points to the sun under the control of the director 21, reflects and focuses the sunlight on the absorber 23, and the absorber 23 converts the sunlight energy into the thermal energy of the heat transfer medium 25. The heat transfer medium 25 carries the heat energy and is transported to the working medium cavity between the reaction chamber shell 11 and the reaction chamber inner cavity 12 under the action of the circulation pump 26, thereby transferring the heat energy to the lunar soil and reaction gas in the reaction chamber inner cavity 12, providing heat energy for the lunar soil oxygen production reaction, and solving the problem of high energy consumption.

[0063] like Figure 5 As shown, Figure 5 The figure is a schematic diagram of the flow path of the lunar soil and slag of the present invention. The present invention adopts a feed bin 31 and a slag bin 34 with transition bin characteristics, which are respectively arranged directly above and directly below the inner cavity 12 of the reaction chamber. The feed valve 32 of the feed bin 31 is opened to load the lunar soil raw material into the feed bin 31, and then the feed valve 32 of the feed bin 31 is closed to maintain the air pressure in the inner cavity 12 of the reaction chamber, and then the discharge valve 33 of the feed bin 31 is opened to allow the lunar soil raw material to gradually flow into the inner cavity 12 of the reaction chamber. The continuous supply of lunar soil is achieved by opening and closing the feed valve 32 and the discharge valve 33 of the feed bin 31 in sequence, while the pressure in the inner cavity 12 of the reaction chamber is kept stable. Similarly, the continuous discharge of slag is achieved by opening and closing the slag inlet valve 35 and the slag outlet valve 36 of the slag bin 34 in sequence, while the air pressure in the inner cavity 12 of the reaction chamber is kept stable, thereby achieving continuous production of the lunar soil oxygen production system.

[0064] like Figure 6 As shown, Figure 6The present invention uses the gas supply and exhaust subsystem 4 to adjust the gas pressure in the reaction chamber inner cavity 12, connects the gas inlet valve 41 and the exhaust valve 42 to the reaction chamber inner cavity 12 through the gas pipe 43, and uses the gas inlet valve 41 and the exhaust valve 42 to regulate the entry of the reaction gas and the discharge of the product gas to achieve the stability of the reaction pressure.

[0065] The present invention adopts the reaction chamber inner cavity 12 with an hourglass-shaped structure. The lunar soil raw material flows from top to bottom in the reaction chamber inner cavity 12 under the action of lunar surface gravity, and the reaction gas flows from bottom to top in the reaction chamber inner cavity 12 under the action of pressure difference. The lunar soil raw material forms an hourglass phenomenon at the connection point of the middle and top vertices of the hourglass-shaped structure, which slows down the falling speed of the lunar soil particles, increases the contact area between the lunar soil raw material particles and the reaction gas, and improves the reaction rate; at the same time, the reaction time of the lunar soil raw material particles and the reaction gas in the reaction chamber inner cavity 12 is extended, so that the reactants react fully, thereby improving the reaction conversion rate.

[0066] The control subsystem 5 of the present invention at least includes a gas pressure gauge 51, a thermocouple 52, a piezoelectric sensor 53, a single-chip microcomputer controller 54 and a servo motor 55. The control subsystem 5 measures the gas pressure in the inner cavity 12 of the reaction chamber through the gas pressure gauge 51, and the single-chip microcomputer controller 54 controls the corresponding devices of the gas supply and exhaust subsystem according to the gas pressure in the inner cavity 12 of the reaction chamber to maintain the gas pressure in the inner cavity 12 of the reaction chamber, that is, the intake flow rate and the exhaust flow rate are regulated by the intake valve 41 and the exhaust valve 42; similarly, the control subsystem 5 measures the temperature in the inner cavity 12 of the reaction chamber through the thermocouple 52, and the single-chip microcomputer controller 54 controls the corresponding devices of the heating subsystem according to the temperature in the inner cavity 12 of the reaction chamber to maintain the temperature in the inner cavity 12 of the reaction chamber, such as regulating the flow rate of the heat transfer medium 25 through the circulation pump 26, or when rapid cooling / turning off is required. When the device is closed, the angle of the orienter is controlled; the control subsystem 5 measures the mass of the lunar soil raw material in the feed bin 31 and the mass of the slag in the slag bin 34 through the piezoelectric sensor 53, and the single-chip controller 54 controls the feed valve 32 and the discharge valve 33 of the feed bin 31 according to the mass of the lunar soil raw material in the feed bin 31, and regulates the discharge (feeding to the inner cavity 12 of the reaction chamber) and the replenishment (replenishment to the feed bin 31) of the lunar soil raw material; the single-chip controller 54 controls the slag inlet valve 35 and the slag discharge valve 36 of the slag bin 34 according to the mass of the slag, and regulates the slag discharge (slag discharge from the inner cavity 12 of the reaction chamber to the slag bin 34) and slag discharge (slag discharge from the slag bin 34 to the outside).

[0067] The reaction chamber subsystem 1 of the present invention is where the lunar soil oxygen production reaction occurs. The bracket 14 provides stable support, the insulation layer 13 reduces heat loss, the reaction chamber shell 11 and the reaction chamber inner cavity 12 constitute the environment in which the reaction occurs. The reaction chamber subsystem 1 is responsible for monitoring and regulating the entire oxygen production process to ensure that the reaction is carried out under optimal conditions.

[0068] Example 2

[0069] The present invention provides a lunar soil oxygen production reactor system, which includes a reaction chamber subsystem 1, a heating subsystem 2, a material supply and slag removal subsystem 3, a gas supply and exhaust subsystem 4 and a control subsystem 5.

[0070] The reaction chamber subsystem 1 provides a lunar soil oxygen production reaction site for the system, and the reaction chamber subsystem 1 includes a reaction chamber shell 11 and a reaction chamber inner cavity 12. Except for the structure of the reaction chamber inner cavity 12, the other structures are the same as those of Example 1.

[0071] The inner cavity 12 of the reaction chamber is a plurality of interconnected spiral tubes, the number of the spiral tubes is 1 to 100 groups, the volume of the inner cavity 12 of the reaction chamber accounts for 10 to 90% of the reaction chamber shell 11, and the arrangement of the spiral tubes is coaxial arrangement and / or parallel axis arrangement. The lunar soil material flows downward from the feed bin 31 at the top of the reaction chamber through the inner cavity 12 of the reaction chamber, reacts with the reaction gas in the inner cavity 12 of the reaction chamber, and then is converted into slag and flows into the slag bin 34 at the bottom of the reaction chamber.

[0072] The specific embodiments described above further illustrate the purpose, technical solutions and beneficial effects of the present invention. It should be understood that the above description is only a specific embodiment of the present invention and is not intended to limit the present invention. It can also be a reasonable combination of the features recorded in the above embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims

1. A lunar soil oxygen production reactor system, characterized in that: include: Reaction chamber subsystem (1), heating subsystem (2), material supply and slag removal subsystem (3), gas supply and exhaust subsystem (4) and control subsystem (5); The reaction chamber subsystem (1) is used to provide a place for the lunar soil oxygen production reaction; The feeding and slag discharge subsystem (3) comprises a feeding bin (31) and a slag bin (34), and both the feeding bin (31) and the slag bin (34) are connected to the reaction chamber inner cavity (12) of the reaction chamber subsystem (1), so as to continuously supply lunar soil raw materials and discharge slag materials to the lunar soil oxygen production reactor system; The gas supply and exhaust subsystem (4) is used to continuously supply reaction gas to the lunar soil oxygen production reactor system and exhaust product gas; The heating subsystem (2) converts sunlight energy into thermal energy of a heat transfer medium (25) via a heat absorber (23), thereby supplying thermal energy to the lunar soil oxygen production reactor system.

2. The lunar soil oxygen production reactor system according to claim 1, characterized in that: The reaction chamber subsystem (1) further comprises a reaction chamber shell (11), the reaction chamber inner cavity (12) being arranged in the reaction chamber shell (11), and a working medium cavity for filling the heat transfer working medium (25) being provided between the reaction chamber shell (11) and the reaction chamber inner cavity (12); The inner cavity (12) of the reaction chamber is a plurality of interconnected hourglass-shaped reaction chambers, or The inner cavity (12) of the reaction chamber is a plurality of interconnected spiral tubes; The arrangement of the multiple hourglass-shaped reaction chambers or the multiple spiral tubes is coaxial arrangement and / or parallel axis arrangement.

3. The lunar soil oxygen production reactor system according to claim 2, characterized in that: The heat supply subsystem (2) further comprises a heat pipe (24), a circulation pump (26) and a reflector (22); the heat pipe (24) connects the circulation pump (26), the heat absorber (23) and the working medium chamber to form a loop.

4. The lunar soil oxygen production reactor system according to claim 1, characterized in that: The feed bin (31) is arranged directly above the inner cavity (12) of the reaction chamber and is in communication with the inner cavity (12) of the reaction chamber, and continuously supplies lunar soil raw materials into the inner cavity (12) of the reaction chamber by gravity; The slag bin (34) is arranged directly below the inner cavity (12) of the reaction chamber and is in communication with the inner cavity (12) of the reaction chamber, so as to discharge the slag continuously by gravity.

5. The lunar soil oxygen production reactor system according to claim 1, characterized in that: The inlet end and the outlet end of the feed bin (31) are respectively provided with a feed valve (32) and a discharge valve (33); A slag inlet valve (35) and a slag outlet valve (36) are provided at the inlet and outlet ends of the slag bin (34).

6. The lunar soil oxygen production reactor system according to claim 5, characterized in that: The air supply and exhaust subsystem (4) comprises an air intake valve (41), an exhaust valve (42) and an air delivery pipe (43); The air inlet valve (41) is arranged at the lower part of the reaction chamber subsystem (1), and the air exhaust valve (42) is arranged at the upper part of the reaction chamber subsystem (1).

7. The lunar soil oxygen production reactor system according to claim 6, characterized in that: The control subsystem (5) is used to control the heat energy supply, lunar soil raw material supply and slag discharge, and gas supply and discharge of the lunar soil oxygen production reactor system; The control subsystem (5) comprises a single-chip microcomputer controller (54), a thermocouple (52), a gas pressure gauge (51) and a piezoelectric sensor (53); the air intake valve (41), the exhaust valve (42), the feed valve (32), the discharge valve (33), the slag feed valve (35) and the slag discharge valve (36) are electrically connected to the single-chip microcomputer controller (54); The thermocouple (52), the gas pressure gauge (51), and the piezoelectric sensor (53) are all electrically connected to the single-chip controller (54).

8. The lunar soil oxygen production reactor system according to claim 7, characterized in that: The heating subsystem (2) is also equipped with a director (21), and the director (21) is controlled by the single-chip controller (54) to point toward the sun, so as to reflect and focus sunlight on the heat absorber (23).

9. The lunar soil oxygen production reactor system according to claim 7, characterized in that: The feed valve (32), the discharge valve (33), the slag feed valve (35) and the slag discharge valve (36) are all equipped with a servo motor (55), and any of the servo motors (55) is electrically connected to the single chip controller (54).

10. The lunar soil oxygen production reactor system according to claim 1, characterized in that: A heat insulation layer (13) is provided on the outer surface of the reaction chamber shell (11).