CN202415191U - Continuous nickel particle dissolving reactor - Google Patents
Continuous nickel particle dissolving reactor Download PDFInfo
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- CN202415191U CN202415191U CN 201220022501 CN201220022501U CN202415191U CN 202415191 U CN202415191 U CN 202415191U CN 201220022501 CN201220022501 CN 201220022501 CN 201220022501 U CN201220022501 U CN 201220022501U CN 202415191 U CN202415191 U CN 202415191U
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- reactor
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- nickel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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Abstract
The utility model relates to a continuous nickel particle dissolving reactor. A mixing tank made from glass fiber reinforced plastic is additionally arranged, and is connected with the middle upper part of a reactor cylinder; solution and acid solution are added into the mixing tank to be mixed with solution circulating in the reactor, and then are heated in a graphite heat exchanger, the mixed solution are sent to a nickel bed in the reactor via an inlet on the bottom of the reactor, after the acid in the solution reacts with the nickel, one part of the solution flows out from an overflow port on the upper end of the reactor cylinder, most part of the solution is sent to the mixing tank and then is sent to the graphite heat exchanger again so as to construct an internal circulation; and the steam of the graphite heat exchanger is introduced via a steam inlet, and the steam condensed water generated after the solution heating process is discharged via a discharging port. According to the structure, internal circulation of solution is established by heating the solution by the graphite solution, so that the contact area between the solution and the nickel particle is enlarged, and the diffusion speed of hydrogen ion and nickel ion is accelerated, and in this way, the dissolving speed of the nickel particles is accelerated, and meanwhile, the product solution is obtained continuously and stably.
Description
Technical field
The utility model relates to a kind of continous way solubilizing reaction equipment, especially relates to the efficient dissolved continous way of a kind of nickel shot nickel shot dissolution reactor.
Background technology
The nickel shot dissolution reactor is a kind of reactor drum of all being participated in mutually by solid, liquid, gas; Usually in a container, add excessive nickel shot and an amount of acid,, make nickel and acid-respons through straight-through steam or steam coils heating; Obtain nickel salt solution; Produce hydrogen simultaneously, drop to the numerical value of expection, then can be considered a batch reaction and accomplish up to the acidity in solution.This reaction is because nickel shot sinks to the bottom of reactor drum, and acid solution adds in the reaction vessel very little with the nickel shot contact area, and solution is difficult to realize stirring, and the nickel ion in the solution is slow with the hydrogen ion diffusion, causes speed of response very slow; Because reactor drum is open, and calorific loss is also very big in the reaction process, cause the energy consumption of LU weight nickel to increase in addition.
Summary of the invention
The utility model technical problem to be solved provides a kind of continous way nickel shot dissolution reactor; Set up the internal recycle of solution; Strengthened the contact area of solution and nickel shot; Improve the velocity of diffusion of hydrogen ion and nickel ion, thereby accelerated nickel shot dissolved speed of response, can continuously, stably obtain product solution simultaneously; This device also easily is automated in addition, improves the procedure quality controlled levels, reduces the input of human capital.
The technical scheme that is adopted that the utility model solves its technical problem is: a kind of continous way nickel shot dissolution reactor; Comprise the reactor shell of making by the glass filament reinforced plastics material; Middle and upper part in said reactor shell one side is provided with a mixing tank; The bottom of said reactor shell one side is provided with graphite heat exchanger, and the middle and upper part, a side of said reactor shell offers spout, offers bottom inlet in a side bottom of reactor shell; The top of said mixing tank offers acid-adding port and second and adds the solution mouth, offers outlet in the bottom of mixing tank; The top of said graphite heat exchanger offers top exit, and the upper and lower part, side of said graphite heat exchanger offers steam-in and relief outlet respectively, and the bottom of said graphite heat exchanger offers inlet; Wherein, said spout is through the pipe connection mixing tank, and said outlet is connected to inlet through circulation tube, and said top exit is through the pipe connection bottom inlet.
Further, the inside of said reactor shell is provided with reactor inner container, seals through the cap that goes in ring between the upper end of this reactor inner container and reactor shell, and the bottom of said reactor inner container is supported and fixed on the intravital bottom of reactor cylinder through acid resisting brick.
In order to guarantee that solution mixes in the bottom, the number of said acid resisting brick is at least four, and the spacing of its adjacent two acid resisting bricks is bigger.
Further, the number of said acid resisting brick is eight.
In order to detect solution acidity, sour flow is advanced in adjustment successively, offers thief hole on the circulation tube of said connection outlet and inlet.
Be acid gas, water vapour and hydrogen collection district that reaction produced on reactor shell top,, the reaction gas that the peak produced played shock absorption, realize the stable state discharging of gas for expansion space; At the reactor shell bottom space is the solution district; For expansion space, help mixing at this through the acid resisting brick space through the solution of inside reactor nickel bed reaction, divide other; It is just horn-like that the top of said reactor shell is, and the bottom of said reactor shell is horn-like.
Further, for the air pressure of controlling reactor barrel, the upper end of said reactor shell also offers emergent venting port.
Further, in order when reactor drum produces fault, to keep in repair or the discharging of solution when stopping production, a side bottommost of said reactor shell offers bottom drain
The beneficial effect of the utility model is: this reasonable in design; Through the graphite heat exchanger heated soln; Set up the internal recycle of solution, strengthened the contact area of solution and nickel shot, improved the velocity of diffusion of hydrogen ion and nickel ion; Thereby accelerated nickel shot dissolved speed of response, can continuously, stably obtain product solution simultaneously; This device also easily is automated in addition, improves the procedure quality controlled levels, reduces the input of human capital.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure: 1; Normal exhaust mouth 2; The nickel mouth of pipe 3; First adds solution mouth 4; Emergent venting port 5; Sealing cover 6; Riser 7; Spout 8; Acid-adding port 9; Second adds solution mouth 10; Upflow tube visor 11; Mixing tank 12; Outlet 13; Bottom inlet 14; Bottom drain 15; Top exit 16; Steam-in 17; Graphite heat exchanger 18; Venting port 19; Inlet 20; Thief hole 21; Acid resisting brick 22; Nickel bed 23; Reactor inner container 24; Cap 25 goes in ring; Reactor shell.
Embodiment
The reactor shell 25 that comprises that the glass filament reinforced plastics material is made as shown in Figure 1; Top at said reactor shell 25 seals through sealing cover 5, and the upper and lower shape of this reactor shell 25 is respectively positive trumpet type enlarging and the enlarging of falling the trumpet type, and last trumpet type is that liquid level is with the upper part; Be acid gas, water vapor and hydrogen collection district that reaction produced; Space enlargement has played shock absorption to the reaction gas that the peak produced, and realizes the stable state discharging of gas; Following trumpet type is the reactor bottom zone; The bottom is evenly distributed with eight acid resisting bricks 21; Have bigger space between adjacent two acid resisting bricks, by the glass filament reinforced plastics material make reactor inner container 23 with regard to frame on acid resisting brick 21,25 belt caps 24 with the glass filament reinforced plastics material of reactor inner container 23 and reactor shell are sealed; The space of reactor shell 25 bottom trumpet types is the solution district; This space is bigger, helps mixing at this through acid resisting brick 21 spaces through the solution of reactor drum nickel bed 22 reactions, and nickel shot adds the nickel mouth of pipe 2 by reactor shell 25 tops and adds; In reactor inner container 23, form nickel bed 22; And keep this nickel bed 22 height, then by first of reactor shell 25 tops add solution mouth 3 add drop arranged in hot water or dilute solution to the upflow tube visor 10 till, this solution that overflows enters in the upflow tube visor 10 via riser 6.
When carrying out solution circulated, begin to feed steam to the steam-in 16 of graphite heat exchanger 17, steam condensate relief outlet 18 is discharged; Because graphite heat exchanger 17 upper and lower ends produce the temperature difference, cause the solution in the interchanger to form thermal siphon, solution is flowed out by the spout 7 of reactor shell 25 middle and upper parts; Get into solution mixing tank 11, flowed into the inlet 19 of graphite heat exchanger 17 bottoms again by outlet 12, the heating back is flowed out by interchanger top exit 15; Bottom inlet 13 by reactor drum gets in the reactor shell 25; Through nickel bed 22, get into mixing tank 11 once more then, set up the internal recycle of reactor drum thus.
When solution temperature is raised to set(ting)value in the question response device; Beginning adds the acid of certain flow at the acid-adding port 8 on mixing tank 11 tops; Add the dilute solution that solution mouth 9 adds certain flow second, through nickel bed 22 and nickel reactant, obtain the rich solution of low acidity, high nickel concentration after added acid and dilute solution are heated by graphite heat exchanger 17; Pipe by the rich solution riser above the reactor drum overflows, the amount balance of the spillage of rich solution and the dilute solution of adding and acid.In this process, the flow of acid and dilute solution, temperature, steam flow etc. can realize automatic control.
Simultaneously, in reaction process, constantly there are acid gas, water vapor and hydrogen to produce; These gases accumulate to the liquid level top, are discharged by the normal exhaust mouth 1 of reactor shell 25 tops, if the gas vol that is produced is big; When pressure is high, can be by emergent venting port 4 one discharge; Thief hole 20 sampling analysis acidity on the solution circulated pipe can be adjusted in view of the above and add sour flow.Simultaneously, offering bottom drain 14 at the bottommost of reactor bottom 25 1 sides, is the drain of solution when being used for reactor drum breakdown maintenance or stopping production.
Claims (8)
1. continous way nickel shot dissolution reactor; Comprise the reactor shell of making by the glass filament reinforced plastics material (25); It is characterized in that: be provided with a mixing tank (11) in the middle and upper part of said reactor shell (25) one sides; The bottom of said reactor shell (25) one sides is provided with graphite heat exchanger (17), and the middle and upper part, a side of said reactor shell (25) offers spout (7), offers bottom inlet (23) in a side bottom of reactor shell (25); The top of said mixing tank (11) offers acid-adding port (8) and second and adds solution mouth (9), offers outlet (12) in the bottom of mixing tank (11); The top of said graphite heat exchanger (17) offers top exit (15); The upper and lower part, side of said graphite heat exchanger (17) offers steam-in (16) and relief outlet (18) respectively, and the bottom of said graphite heat exchanger (17) offers inlet (19); Wherein, said spout (7) is through pipe connection mixing tank (11), and said outlet (12) is connected to inlet (19) through circulation tube, and said top exit (15) is through pipe connection bottom inlet (13).
2. continous way nickel shot dissolution reactor according to claim 1; It is characterized in that: the inside of said reactor shell (25) is provided with reactor inner container (23); Seal through the cap (24) that goes in ring between upper end of this reactor inner container (23) and reactor shell (25), the bottom of said reactor inner container (23) is supported and fixed on the bottom in the reactor shell (25) through acid resisting brick (21).
3. continous way nickel shot dissolution reactor according to claim 2 is characterized in that: the number of said acid resisting brick (21) is at least four, and the spacing of its adjacent two acid resisting bricks (21) is bigger.
4. continous way nickel shot dissolution reactor according to claim 3 is characterized in that: the number of said acid resisting brick (21) is eight.
5. continous way nickel shot dissolution reactor according to claim 1 is characterized in that: offer thief hole (20) on the circulation tube of said connection outlet (12) and inlet (19).
6. continous way nickel shot dissolution reactor according to claim 1 and 2 is characterized in that: the top of said reactor shell (25) is just horn-like, and the bottom of said reactor shell (25) is horn-like.
7. according to its claim 1 or 2 described continous way nickel shot dissolution reactor, it is characterized in that: the upper end of said reactor shell (25) also offers emergent venting port (4).
8. continous way nickel shot dissolution reactor according to claim 1 and 2 is characterized in that: a side bottommost of said reactor shell (25) offers bottom drain (14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220022501 CN202415191U (en) | 2012-01-18 | 2012-01-18 | Continuous nickel particle dissolving reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220022501 CN202415191U (en) | 2012-01-18 | 2012-01-18 | Continuous nickel particle dissolving reactor |
Publications (1)
Publication Number | Publication Date |
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CN202415191U true CN202415191U (en) | 2012-09-05 |
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CN 201220022501 Expired - Fee Related CN202415191U (en) | 2012-01-18 | 2012-01-18 | Continuous nickel particle dissolving reactor |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107362757A (en) * | 2017-08-25 | 2017-11-21 | 江西艾德纳米科技有限公司 | It is a kind of prepare metal salt continuously generate reaction unit and preparation method |
CN112665920A (en) * | 2020-12-19 | 2021-04-16 | 北京大学 | Automatic monitoring system for liquid phase synthesis |
-
2012
- 2012-01-18 CN CN 201220022501 patent/CN202415191U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107362757A (en) * | 2017-08-25 | 2017-11-21 | 江西艾德纳米科技有限公司 | It is a kind of prepare metal salt continuously generate reaction unit and preparation method |
CN112665920A (en) * | 2020-12-19 | 2021-04-16 | 北京大学 | Automatic monitoring system for liquid phase synthesis |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120905 Termination date: 20150118 |
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EXPY | Termination of patent right or utility model |