EP3388619A1 - System for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits - Google Patents
System for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits Download PDFInfo
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- EP3388619A1 EP3388619A1 EP18152415.8A EP18152415A EP3388619A1 EP 3388619 A1 EP3388619 A1 EP 3388619A1 EP 18152415 A EP18152415 A EP 18152415A EP 3388619 A1 EP3388619 A1 EP 3388619A1
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- Prior art keywords
- hydrothermal
- fluid
- well casing
- mixing control
- fluid mixing
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- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000003306 harvesting Methods 0.000 title claims abstract description 22
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 19
- 239000012530 fluid Substances 0.000 claims abstract description 102
- 238000002156 mixing Methods 0.000 claims abstract description 48
- 239000011248 coating agent Substances 0.000 claims abstract description 7
- 238000000576 coating method Methods 0.000 claims abstract description 7
- 238000005553 drilling Methods 0.000 claims description 27
- 239000002245 particle Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 5
- 239000004568 cement Substances 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 150000004763 sulfides Chemical class 0.000 description 12
- 239000013535 sea water Substances 0.000 description 10
- 229910052500 inorganic mineral Inorganic materials 0.000 description 8
- 239000011707 mineral Substances 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 7
- 239000010949 copper Substances 0.000 description 7
- 239000011701 zinc Substances 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052925 anhydrite Inorganic materials 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 229910017052 cobalt Inorganic materials 0.000 description 4
- 239000010941 cobalt Substances 0.000 description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 4
- 230000008021 deposition Effects 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 230000006911 nucleation Effects 0.000 description 4
- 238000010899 nucleation Methods 0.000 description 4
- 229910052569 sulfide mineral Inorganic materials 0.000 description 4
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 4
- 206010039509 Scab Diseases 0.000 description 3
- 230000033558 biomineral tissue development Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000002708 enhancing effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000012827 research and development Methods 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 229910017827 Cu—Fe Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052960 marcasite Inorganic materials 0.000 description 1
- 239000002366 mineral element Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000011022 opal Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21C—MINING OR QUARRYING
- E21C50/00—Obtaining minerals from underwater, not otherwise provided for
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/01—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells specially adapted for obtaining from underwater installations
Definitions
- the present invention relates to the technical field of exploration and exploitation of deep-sea metallic sulfides, in particular to a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits.
- Deep-sea hydrothermal metallic sulfide deposits are metallic mineral resources with a strategic significance in modern times, including metallic elements such as iron, copper, lead, zinc, nickel, cobalt, gold, silver, platinum. Those deposits are distributed in global oceans from hundreds of meters to 4,000 meters deep, and are mainly focused at mid-ocean ridges, back-arc basins and formation mobile fault zones. According to preliminary estimates, some 900 individual hydrothermal metallic sulfide deposits are totally cultivated at the sea floors of the oceans in the world, and some 160 deposits have been found at present. The preliminary estimates on the deposits at several mid-ocean ridges show that the scale usually ranges from 1 million tons to 0.1 billion tons, which reflects that hydrothermal deposits have a considerable resource inventory.
- the sea-floor hydrothermal sulfides Compared with deep-sea polymetallic nodules or cobalt-rich crusts, the sea-floor hydrothermal sulfides have advantages of small water depth, high quality, easy exploitation, beneficiation and smelting. Therefore, the investigation, research and development activities are significant for human society which faces resources shortages increasingly.
- the objective of the present invention is to provide a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits, which makes a full use of the natural factors to harvest the deep-sea hydrothermal metallic sulfide deposits so as to reduce the exploitation cost and avoid environmental pollution.
- the present invention provides a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits.
- the system includes a well casing, a well head flow control device, a fluid mixing control hood; the well casing being configured to penetrate into a hydrothermal metallic sulfide deposit mound body including a confining layer, a hydrothermal fluid enriching layer and mound body bedrock consecutively from the outside to the inside; perforations are formed at a casing wall of the well casing that is configured to be positioned at the hydrothermal fluid enriching layer;
- the well head flow control device is provided at the top of the well casing; a lower opening is formed at the bottom of the fluid mixing control hood; the lower opening surrounds the top of the well casing; an upper opening is formed at the top of the fluid mixing control hood; a plurality of fluid holes are formed at a lateral wall of the fluid mixing control hood; and a sulfide coating is applied to the inner wall of the fluid
- the well head flow control device may comprise a barometric flow control valve and a fluid temperature sensor; the barometric flow control valve may be disposed on the well casing; and a temperature sensing end of the fluid temperature sensor may be disposed at an outlet of the top of the well casing.
- the fluid mixing control hood may have a round table structure; a lower round opening may be formed in the center of the round bottom face of the fluid mixing control hood with the round table structure; and an upper round opening may be formed at a sharp tip of the fluid mixing control hood with the round table structure.
- the round bottom face of the fluid mixing control hood with the round table structure may have a diameter of 16m and a height of 20m; the lower round opening may have a diameter of 6m, and the upper round opening may have a diameter of 4m.
- a stainless steel outer layer may be disposed on the outer wall of the fluid mixing control hood.
- a large particle filtering screen may be disposed at the outlet of the top of the well casing.
- a well head support configured to be erected on the sea floor may be disposed at the top of the well casing.
- the well casing may be reinforced with a cement well wall on the outer side.
- the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits may also comprise a mobile drilling platform; the mobile drilling platform may be configured to exploit and drill the hydrothermal metallic sulfide mound body by using a drill stem to form a natural well; and to insert the well casing into the natural well to run through the hydrothermal metallic sulfide mound body.
- the mobile drilling platform may comprise a drilling engineering ship and a drilling platform which is disposed on the drilling engineering ship.
- the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits of the present invention has the following features and advantages:
- Hydrothermal black smoker chimneys of sea-floor metallic sulfide deposits are formed after high-temperature, reducing hydrothermal fluid 8 that contains metallic elements such as iron, copper and zinc and erupts from a hydrothermal spout of a hydrothermal metallic sulfide mound body 12 is mixed with the surrounding cold, oxidizing sea water 7 and then performs deposition.
- a "separation" effect occurs in the lower reacting zone, so the high-temperature hydrothermal fluid 8 has very high buoyancy in comparison with the sea water 7 and therefore can quickly erupt from the sea floor.
- the main products are black smoker chimneys constituted by copper-rich sulfides and sulfates; when the temperature of the high-temperature hydrothermal fluid 8 is within the range of 100-350°C, the main products are white smoker chimneys constituted by silicious substances, sulfates and a small amount of Zn-rich sulfides and marcasite.
- Annular anhydrite deposits generated around the spout retard the direct mixing between the hydrothermal liquid and the sea water 7, and provide a base for the deposition of other minerals; stage 2, in a channel formed by the annular anhydrite, copper pyrites (CuFeS2) start to deposit, while the hydrothermal fluid 8 and the sea water 7 diffuse and flow toward each other through the newly formed, puffed, porous chimney wall.
- CuFeS2 copper pyrites
- this embodiment provides a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits, which simulates the low-temperature gypsum and sulfate outer wall formed in the early stage, and achieves the objective of controlling the temperature of the fluid in the chimney and the growth rate of the minerals.
- the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits in this embodiment includes functional units such as a mobile drilling platform, a well casing 10, a well head control flow guide device 9 and a fluid mixing control hood 3.
- the mobile drilling platform includes a drilling engineering ship 1 and a drilling platform 2 disposed on the drilling engineering ship 1; the drilling platform 2 drills a hydrothermal metallic sulfide mound body 12 by using a drilling stem to form a natural well 98; and the well casing 10 is inserted into the natural well 98 to run through the hydrothermal metallic sulfide mound body 12.
- the hydrothermal metallic sulfide deposit mound body 12 includes a confining layer 13, a hydrothermal fluid enriching layer 14 and mound body bedrock 15 in turn from the outside to the inside, and perforations 11 are formed at the casing wall of the well casing 10 that is positioned at the hydrothermal fluid enriching layer 14.
- a well head flow control device 9 is disposed at the top of the well casing 10.
- the well head control flow control device 9 includes a barometric flow control valve 93 and a fluid temperature sensor 94; the barometric flow control valve 93 is disposed on the well casing 10 and is configured on a valve instrument console 92; and a temperature sensing end of the fluid temperature sensor 94 is disposed at an outlet of the top of the well casing 10.
- a large particle filtering screen 96 is disposed at the outlet of the top of the well casing 10; a hydrothermal fluid spout 91 is connected to the well casing 10; a well head support 95 which is erected on the sea floor 99 is disposed at the top of the well casing 10; and a cement well wall 97 is disposed between the outer side of the well casing 10 and the natural well 98.
- the fluid mixing control hood 3 has a round table structure; a lower round opening is formed in the center of the round bottom face of the fluid mixing control hood 3 with the round table structure; an upper round opening 4 is formed at a sharp tip of the fluid mixing control hood 3 with the round table structure; and a stainless steel outer layer with a thickness of 2cm is disposed on the outer wall of the fluid mixing control hood 3.
- the round bottom face of the fluid mixing control hood 3 with the round table structure has a diameter of 16m and a height of 20m; the lower round opening has a diameter of 6m, and the upper round opening 4 has a diameter of 4m.
- the lower opening of the fluid mixing control hood 3 surrounds the top of the well casing 10; the upper opening 4 is formed at the top of the fluid mixing control hood 3; a plurality of fluid holes 6 are formed on a lateral wall of the fluid mixing control hood 3; the sizes and quantity of the fluid holes 6 can be regulated according to the flow rate and temperature of the hydrothermal fluid 8; hotter hydrothermal fluid 8 leads to larger and more fluid holes 6; vice versa, smaller and fewer holes are obtained.
- the surrounding cold sea water 7 can enter via the fluid holes 6 to be mixed with the high-temperature hydrothermal fluid 8 in the fluid mixing control hood 3.
- a sulfide mineral coating 5 with a thickness of 1cm is applied to the inner wall of the fluid mixing control hood 3, for example pyrites, copper pyrites, lead zinc ores and zinc blends, so as to control the generation of the mineral elements in the principle of nucleation induction.
- the fluid mixing control hood 3 can overall reduce the rate of diffusion of the high-temperature hydrothermal fluid 8 towards the sea water 7 in the surroundings, keep a relatively high temperature such that the hydrothermal fluid 8 quickly nucleates to form minerals on the sulfide mineral coating 5, and at the same time, effectively reduce the ratio of the low-temperature minerals (such as gypsum and opal) with a relatively poor economic significance, thus making sure that a high-temperature fluid channel is formed in the center in the early stage of mineralization, and ensuring that the fluid on the floor is continuously supplied upward via the well casing 10.
- the low-temperature minerals such as gypsum and opal
- the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits performs production according to the following procedure: with the support of the drilling engineering ship 1, the drilling platform 2 drills the hydrothermal metallic sulfide mount body 12, pierces the confining layer 13, enters the hydrothermal fluid enriching layer 14, and usually at last, needs to form the natural well 98 at the end hole of the mound body bedrock 15. After finishing drilling, the drilling stem retracts.
- the drilling stem shown in FIG.1 is mainly illustrative, and is not included in the subsequent system.
- the well casing 10 is inserted into the natural well 98 to run through the hydrothermal metallic sulfide mount body 12, and guided by the perforations 11 at the hydrothermal fluid enriching layer 14, the hydrothermal fluid 8 enters the well casing 10.
- the hydrothermal fluid 8 enters the fluid mixing control hood 3 via the well head control flow guide device 9.
- the flow rate and pressure of the hydrothermal fluid 8 can be regulated with the barometric flow control valve 93 in the well head control flow guide device 9 so as to obtain the optimal hydrothermal fluid 8.
- the temperature of the hydrothermal fluid 8 can be measured in situ with the fluid temperature meter 94 so as to facilitate the selection of the fluid mixing control hood 3 with proper sizes and density of the fluid holes 6, thus ensuring effective control over the mixing process of the surrounding sea water 7 and the hydrothermal fluid 8, maintaining a certain temperature in the fluid mixing control hood 3, and ensuring fast nucleation and mineralization on the inner sulfide mineral coating 5.
- the round bottom face of the fluid mixing control hood 3 with the round table structure has a diameter of 16m and a height of 20m; the lower round opening has a diameter of 6m, and the upper round opening 4 has a diameter of 4m.
- the fluid mixing control hold 3 can be distributed and placed with a sea-floor engineering robot. After one harvesting cycle is finished, the cutting of the hood bottom of the fluid mixing control hood 3 can be automatically controlled with the engineering robot, and then round table-shaped sulfide minerals can be hoisted to the sea level with the engineering ship platform, thus completing a harvesting cycle.
- the in-situ harvesting system of deep-sea hydrothermal metallic sulfide deposits does not need any maintenance cost in the growth process except for some cost in the launching and cutting procedures. Large-scale submarine exploitation is not needed, so the environmental risks are greatly reduced.
- nucleation can be induced through controlling factors such as temperature, flow rate and pressure of the mixed fluids, capable of effectively improving the mineral quality, enhancing the contents of elements including Cu, Zn and Fe, and enhancing economic benefits.
- Considerable benefits can be obtained if dozens or hundreds of deep-sea hydrothermal metallic sulfide deposits are harvested in a common hydrothermal fluid field (some hundreds of square meters to several square kilometers) at the same time.
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Abstract
Description
- The present invention relates to the technical field of exploration and exploitation of deep-sea metallic sulfides, in particular to a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits.
- Deep-sea hydrothermal metallic sulfide deposits are metallic mineral resources with a strategic significance in modern times, including metallic elements such as iron, copper, lead, zinc, nickel, cobalt, gold, silver, platinum. Those deposits are distributed in global oceans from hundreds of meters to 4,000 meters deep, and are mainly focused at mid-ocean ridges, back-arc basins and formation mobile fault zones. According to preliminary estimates, some 900 individual hydrothermal metallic sulfide deposits are totally cultivated at the sea floors of the oceans in the world, and some 160 deposits have been found at present. The preliminary estimates on the deposits at several mid-ocean ridges show that the scale usually ranges from 1 million tons to 0.1 billion tons, which reflects that hydrothermal deposits have a considerable resource inventory. Compared with deep-sea polymetallic nodules or cobalt-rich crusts, the sea-floor hydrothermal sulfides have advantages of small water depth, high quality, easy exploitation, beneficiation and smelting. Therefore, the investigation, research and development activities are significant for human society which faces resources shortages increasingly.
- In the 1960s, the development of sea-floor metallic sources boomed, including polymetallic nodules, cobalt-rich crusts and hydrothermal metallic sulfide deposits. A great progress has been made after decades of research and development. Even so, there are still difficulties in the exploitation of the deep-sea metallic sulfides at present, mainly including the following aspects. 1) High exploitation cost: The quality of the sea-floor sulfides is high, but if the sea-floor sulfides does not reach a certain exploitation scale, the cost is inevitably higher than the land exploitation, and the cost in the ore transport and in the recycling and smelting of metals such as silver, copper, zinc, lead, etc. are also relatively high. 2) Conventional concept and immature technologies: The exploitation technologies and experience of the deep-sea polymetallic nodules, cobalt-rich crusts and deep-sea oil gases can only serve as references of the exploitation of the hydrothermal sulfides, so new approaches are in need, and aiming at the formation features of the sea-floor deposit, innovative ideas are required to design more reasonable and pertinent exploration and exploitation solutions. 3) Environmental risks: Once submarine mining enters the implementation stage, risks will be inevitably brought to the marine environment, including water pollution and submarine landslide, in particular possible damage to the unique biotic and ecological communities of the hydrothermal zones, thus resulting in ecological disasters.
- The objective of the present invention is to provide a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits, which makes a full use of the natural factors to harvest the deep-sea hydrothermal metallic sulfide deposits so as to reduce the exploitation cost and avoid environmental pollution.
- The present invention provides a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits. The system includes a well casing, a well head flow control device, a fluid mixing control hood; the well casing being configured to penetrate into a hydrothermal metallic sulfide deposit mound body including a confining layer, a hydrothermal fluid enriching layer and mound body bedrock consecutively from the outside to the inside; perforations are formed at a casing wall of the well casing that is configured to be positioned at the hydrothermal fluid enriching layer; the well head flow control device is provided at the top of the well casing; a lower opening is formed at the bottom of the fluid mixing control hood; the lower opening surrounds the top of the well casing; an upper opening is formed at the top of the fluid mixing control hood; a plurality of fluid holes are formed at a lateral wall of the fluid mixing control hood; and a sulfide coating is applied to the inner wall of the fluid mixing control hood.
- Further, the well head flow control device may comprise a barometric flow control valve and a fluid temperature sensor; the barometric flow control valve may be disposed on the well casing; and a temperature sensing end of the fluid temperature sensor may be disposed at an outlet of the top of the well casing.
- Further, the fluid mixing control hood may have a round table structure; a lower round opening may be formed in the center of the round bottom face of the fluid mixing control hood with the round table structure; and an upper round opening may be formed at a sharp tip of the fluid mixing control hood with the round table structure.
- Further, the round bottom face of the fluid mixing control hood with the round table structure may have a diameter of 16m and a height of 20m; the lower round opening may have a diameter of 6m, and the upper round opening may have a diameter of 4m.
- Further, a stainless steel outer layer may be disposed on the outer wall of the fluid mixing control hood.
- Further, a large particle filtering screen may be disposed at the outlet of the top of the well casing.
- Further, a well head support configured to be erected on the sea floor may be disposed at the top of the well casing.
- Further, the well casing may be reinforced with a cement well wall on the outer side.
- Further, the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits may also comprise a mobile drilling platform; the mobile drilling platform may be configured to exploit and drill the hydrothermal metallic sulfide mound body by using a drill stem to form a natural well; and to insert the well casing into the natural well to run through the hydrothermal metallic sulfide mound body.
- Further, the mobile drilling platform may comprise a drilling engineering ship and a drilling platform which is disposed on the drilling engineering ship.
- Compared with the prior art, the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits of the present invention has the following features and advantages:
- 1. The system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits of the present invention induces nucleation through control over factors such as the temperature, flow rate and pressure of mixed fluids, capable of effectively improving ore quality and enhancing economic benefits.
- 2. The system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits of the present invention makes a full use of the natural factors to cultivate the deep-sea hydrothermal metallic sulfide deposits, without any maintenance cost in the growth process.
- 3. The system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits of the present invention does not need large-scale sea-floor exploitation, greatly reduces environmental risks, and avoids environmental pollution.
- The features of the advantages of the present invention become more apparent and clear when read in conjunction with the embodiments of the present invention.
- The present utility model is detailed in conjunction with the drawings and the embodiments below.
- To clearly describe the technical solution in the embodiments of the present disclosure or in the prior art, the following are brief introduction of the attached drawings used to describe the technology in the embodiments or in the prior art. Obviously, the attached drawings described below involve some embodiments of the present disclosure. For those originally skilled in this art, other drawings can be made according to those drawings without creative labor.
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FIG. 1 is a schematic view of in-situ harvesting system of deep-sea hydrothermal metallic sulfide deposits in an embodiment of the present invention; -
FIG. 2 is a schematic view of a part structure of in-situ harvesting system of deep-sea hydrothermal metallic sulfide deposits in an embodiment of the present invention; -
FIG. 3 is a schematic view of a fluid mixing control hood in an embodiment of the present invention; - In the drawings, 1- drilling engineering ship; 2- drilling platform; 3- fluid mixing control hood; 4- upper opening; 5-sulfide coating; 6-fluid hole; 7-sea water; 8-hydrothermal fluid; 9- well head control flow guide control device; 91- hydrothermal fluid nozzle; 92- valve instrument console; 93-barometric flow control valve; 94- fluid temperature sensor; 95- well head support; 96- large particle filtering screen; 97- cement well wall; 98- natural well; 99- sea floor; 10- well casing; 11-perforation; 12-hydrothermal metallic sulfide mound body; 13- confining layer; 14-hydrothermal fluid enriching layer; 15- mound body bedrock.
- Hydrothermal black smoker chimneys of sea-floor metallic sulfide deposits are formed after high-temperature, reducing hydrothermal fluid 8 that contains metallic elements such as iron, copper and zinc and erupts from a hydrothermal spout of a hydrothermal metallic sulfide mound body 12 is mixed with the surrounding cold, oxidizing sea water 7 and then performs deposition. A "separation" effect occurs in the lower reacting zone, so the high-temperature hydrothermal fluid 8 has very high buoyancy in comparison with the sea water 7 and therefore can quickly erupt from the sea floor. When the temperature of the high-temperature hydrothermal fluid 8 is higher than 350°C, the main products are black smoker chimneys constituted by copper-rich sulfides and sulfates; when the temperature of the high-temperature hydrothermal fluid 8 is within the range of 100-350°C, the main products are white smoker chimneys constituted by silicious substances, sulfates and a small amount of Zn-rich sulfides and marcasite.
- The model established after study on the black smoker chimneys in the 21 °N EPR region is still used today. This model represents that the formation of the smoker chimneys is obviously divided into two stages: first, when the high-temperature hydrothermal fluid 8 which has weak acidity and is rich in metals, sulfides and Ca is mixed with the surrounding cold (some 2°C) sea water 7 which has weak alkalinity and is insufficient in metals and sulfates and rich in Ca, anhydrite (CaSO4) and fine Fe, Zn as well as Cu-Fe metallic sulfides perform deposition. Annular anhydrite deposits generated around the spout retard the direct mixing between the hydrothermal liquid and the sea water 7, and provide a base for the deposition of other minerals; stage 2, in a channel formed by the annular anhydrite, copper pyrites (CuFeS2) start to deposit, while the hydrothermal fluid 8 and the sea water 7 diffuse and flow toward each other through the newly formed, puffed, porous chimney wall. In the above-mentioned processes, the sulfides and sulfates are saturated and deposited in pores of the chimney wall, so the permeability of the chimney wall is lowered. Under the condition that the chimney channel keeps smooth continuously, a part of the fluid flows through the top and enters the sea water 7, forming relatively large-scale hydrothermal plumes and resulting in deposition of a large amount of minerals. Thus, a complete hydrothermal chimney is formed.
- According to the above mineralization principle, in order to achieve the objectives of controlling the chimney growth and facilitating exploitation, this embodiment provides a system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits, which simulates the low-temperature gypsum and sulfate outer wall formed in the early stage, and achieves the objective of controlling the temperature of the fluid in the chimney and the growth rate of the minerals. The system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits in this embodiment includes functional units such as a mobile drilling platform, a well casing 10, a well head control flow guide device 9 and a fluid
mixing control hood 3. - As shown in
FIG. 1-FIG. 3 , the mobile drilling platform includes a drilling engineering ship 1 and a drilling platform 2 disposed on the drilling engineering ship 1; the drilling platform 2 drills a hydrothermal metallic sulfide mound body 12 by using a drilling stem to form anatural well 98; and the well casing 10 is inserted into thenatural well 98 to run through the hydrothermal metallic sulfide mound body 12. The hydrothermal metallic sulfide deposit mound body 12 includes a confining layer 13, a hydrothermal fluid enriching layer 14 and mound body bedrock 15 in turn from the outside to the inside, and perforations 11 are formed at the casing wall of the well casing 10 that is positioned at the hydrothermal fluid enriching layer 14. A well head flow control device 9 is disposed at the top of the well casing 10. The well head control flow control device 9 includes a barometric flow control valve 93 and a fluid temperature sensor 94; the barometric flow control valve 93 is disposed on the well casing 10 and is configured on a valve instrument console 92; and a temperature sensing end of the fluid temperature sensor 94 is disposed at an outlet of the top of the well casing 10. A large particle filtering screen 96 is disposed at the outlet of the top of the well casing 10; a hydrothermal fluid spout 91 is connected to the well casing 10; a well head support 95 which is erected on thesea floor 99 is disposed at the top of the well casing 10; and acement well wall 97 is disposed between the outer side of the well casing 10 and thenatural well 98. The fluidmixing control hood 3 has a round table structure; a lower round opening is formed in the center of the round bottom face of the fluidmixing control hood 3 with the round table structure; an upper round opening 4 is formed at a sharp tip of the fluidmixing control hood 3 with the round table structure; and a stainless steel outer layer with a thickness of 2cm is disposed on the outer wall of the fluidmixing control hood 3. In this embodiment, the round bottom face of the fluidmixing control hood 3 with the round table structure has a diameter of 16m and a height of 20m; the lower round opening has a diameter of 6m, and the upper round opening 4 has a diameter of 4m. The lower opening of the fluidmixing control hood 3 surrounds the top of the well casing 10; the upper opening 4 is formed at the top of the fluidmixing control hood 3; a plurality of fluid holes 6 are formed on a lateral wall of the fluidmixing control hood 3; the sizes and quantity of the fluid holes 6 can be regulated according to the flow rate and temperature of the hydrothermal fluid 8; hotter hydrothermal fluid 8 leads to larger and more fluid holes 6; vice versa, smaller and fewer holes are obtained. The surrounding cold sea water 7 can enter via the fluid holes 6 to be mixed with the high-temperature hydrothermal fluid 8 in the fluid mixingcontrol hood 3. Asulfide mineral coating 5 with a thickness of 1cm is applied to the inner wall of the fluid mixingcontrol hood 3, for example pyrites, copper pyrites, lead zinc ores and zinc blends, so as to control the generation of the mineral elements in the principle of nucleation induction. The fluidmixing control hood 3 can overall reduce the rate of diffusion of the high-temperature hydrothermal fluid 8 towards the sea water 7 in the surroundings, keep a relatively high temperature such that the hydrothermal fluid 8 quickly nucleates to form minerals on thesulfide mineral coating 5, and at the same time, effectively reduce the ratio of the low-temperature minerals (such as gypsum and opal) with a relatively poor economic significance, thus making sure that a high-temperature fluid channel is formed in the center in the early stage of mineralization, and ensuring that the fluid on the floor is continuously supplied upward via the well casing 10. - In this embodiment, the system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits performs production according to the following procedure: with the support of the drilling engineering ship 1, the drilling platform 2 drills the hydrothermal metallic sulfide mount body 12, pierces the confining layer 13, enters the hydrothermal fluid enriching layer 14, and usually at last, needs to form the
natural well 98 at the end hole of the mound body bedrock 15. After finishing drilling, the drilling stem retracts. The drilling stem shown inFIG.1 is mainly illustrative, and is not included in the subsequent system. The well casing 10 is inserted into thenatural well 98 to run through the hydrothermal metallic sulfide mount body 12, and guided by the perforations 11 at the hydrothermal fluid enriching layer 14, the hydrothermal fluid 8 enters the well casing 10. After the large particle filtering screen 96 screens out large particles which may block the well casing 10, the hydrothermal fluid 8 enters the fluid mixingcontrol hood 3 via the well head control flow guide device 9. The flow rate and pressure of the hydrothermal fluid 8 can be regulated with the barometric flow control valve 93 in the well head control flow guide device 9 so as to obtain the optimal hydrothermal fluid 8. In addition, the temperature of the hydrothermal fluid 8 can be measured in situ with the fluid temperature meter 94 so as to facilitate the selection of the fluid mixingcontrol hood 3 with proper sizes and density of the fluid holes 6, thus ensuring effective control over the mixing process of the surrounding sea water 7 and the hydrothermal fluid 8, maintaining a certain temperature in the fluid mixingcontrol hood 3, and ensuring fast nucleation and mineralization on the innersulfide mineral coating 5. In this embodiment, the round bottom face of the fluid mixingcontrol hood 3 with the round table structure has a diameter of 16m and a height of 20m; the lower round opening has a diameter of 6m, and the upper round opening 4 has a diameter of 4m. When the temperature of high-temperature fluid is greater than 300 DEG C, it is predicted that it takes some 6-12 months to fully fill the metallic sulfides in the fluid mixingcontrol hood 3. After the drilling is completed, the fluid mixing control hold 3 can be distributed and placed with a sea-floor engineering robot. After one harvesting cycle is finished, the cutting of the hood bottom of the fluid mixingcontrol hood 3 can be automatically controlled with the engineering robot, and then round table-shaped sulfide minerals can be hoisted to the sea level with the engineering ship platform, thus completing a harvesting cycle. - In this embodiment, the in-situ harvesting system of deep-sea hydrothermal metallic sulfide deposits does not need any maintenance cost in the growth process except for some cost in the launching and cutting procedures. Large-scale submarine exploitation is not needed, so the environmental risks are greatly reduced. In addition, nucleation can be induced through controlling factors such as temperature, flow rate and pressure of the mixed fluids, capable of effectively improving the mineral quality, enhancing the contents of elements including Cu, Zn and Fe, and enhancing economic benefits. Considerable benefits can be obtained if dozens or hundreds of deep-sea hydrothermal metallic sulfide deposits are harvested in a common hydrothermal fluid field (some hundreds of square meters to several square kilometers) at the same time. The proposal and application of the in-situ harvesting system of deep-sea hydrothermal metallic sulfide deposits is a symbol that humans enter an integrated harvesting stage of exploring and exploiting the deep-sea mineral products, where more controls can be implemented, leaving a nomadic stage involving much guesswork.
- The above description does not limit the present invention. The present invention is not limited to the above embodiments. All changes, modifications, additions or replacements made by those skilled in the art within the principle of the present invention shall also fall within the protective scope of the present invention
Claims (10)
- A system for in-situ harvesting of deep-sea hydrothermal metallic sulfide deposits, characterized by comprising a well casing (10), a well head flow control device (9), a fluid mixing control hood (3); the well casing (10) being configured to penetrate into a hydrothermal metallic sulfide deposit mound body (12) comprising a confining layer (13), a hydrothermal fluid enriching layer (14) and mound body bedrock (15) consecutively from the outside to the inside; perforations (11) are formed at a casing wall of the well casing (10) that is configured to be positioned at the hydrothermal fluid enriching layer (14); the well head flow control device (9) is provided at the top of the well casing (10); a lower opening is formed at the bottom of the fluid mixing control hood (3); the lower opening surrounds the top of the well casing (10); an upper opening (4) is formed at the top of the fluid mixing control hood (3); a plurality of fluid holes (6) are formed at a lateral wall of the fluid mixing control hood (3); and a sulfide coating (5) is applied to the inner wall of the fluid mixing control hood (3).
- The system according to claim 1, characterized in that the well head flow control device (9) comprises a barometric flow control valve (93) and a fluid temperature sensor (94); the barometric flow control valve (93) is disposed on the well casing (10); and a temperature sensing end of the fluid temperature sensor (94) is disposed at an outlet at the top of the well casing (10).
- The system according to any one of claims 1 or 2, characterized in that the fluid mixing control hood (3) has a round table structure; a lower round opening is formed in the center of the round bottom face of the fluid mixing control hood with the round table structure; and an upper round opening (4) is formed at a sharp tip of the fluid mixing control hood (3) with the round table structure.
- The system according to claim 3, characterized in that the round bottom face of the fluid mixing control hood (3) with the round table structure has a diameter of 16m and a height of 20m; the lower round opening has a diameter of 6m, and the upper round opening has a diameter of 4m.
- The system according to any one of claims 1 to 4, characterized in that a stainless steel outer layer is disposed on the outer wall of the fluid mixing control hood (3).
- The system according to any one of claims 1 to 5, characterized in that a large particle filtering screen (96) is disposed at an outlet of the top of the well casing (10).
- The system according to any one of claims 1 to 6, characterized in that a well head support (95) configured to be erected on the sea floor (99) is disposed at the top of the well casing (10).
- The system according to any one of claims 1 to 7, characterized in that the well casing (10) is reinforced with a cement well wall (97) on the outer side.
- The system according to any one of claims 1-8, characterized by also comprising a mobile drilling platform; the mobile drilling platform being configured to exploit and drill the hydrothermal metallic sulfide mound body (12) by using a drill stem to form a natural well (98); and to insert the well casing (10) into the natural well (98) to run through the hydrothermal metallic sulfide mound body (12).
- The system according to claim 9, characterized in that the mobile drilling platform comprises a drilling engineering ship (1) and a drilling platform (2) which is disposed on the drilling engineering ship (1).
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CN109283179A (en) * | 2018-11-19 | 2019-01-29 | 国家海洋局第二海洋研究所 | Self-tolerant submarine hydrothermal solution plume in-situ detector |
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CN107100627B (en) * | 2017-04-10 | 2018-04-13 | 青岛海洋地质研究所 | Deep-sea hydrothermal metal sulfide mineral deposit original position implant system |
CN115637981B (en) * | 2022-11-01 | 2023-05-02 | 青岛海洋地质研究所 | In-situ operation method for improving ore-forming efficiency of submarine hydrothermal sulfide gold element |
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