CN111921345A - Deuterium gas generator heavy water recovery device - Google Patents

Deuterium gas generator heavy water recovery device Download PDF

Info

Publication number
CN111921345A
CN111921345A CN202010828705.8A CN202010828705A CN111921345A CN 111921345 A CN111921345 A CN 111921345A CN 202010828705 A CN202010828705 A CN 202010828705A CN 111921345 A CN111921345 A CN 111921345A
Authority
CN
China
Prior art keywords
heavy water
metal
clamping plate
gas generator
diaphragm
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202010828705.8A
Other languages
Chinese (zh)
Inventor
王占阳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shenzhen Ruilin Technology Co ltd
Original Assignee
Shenzhen Ruilin Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shenzhen Ruilin Technology Co ltd filed Critical Shenzhen Ruilin Technology Co ltd
Priority to CN202010828705.8A priority Critical patent/CN111921345A/en
Publication of CN111921345A publication Critical patent/CN111921345A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B01D53/228Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00Operating or servicing cells
    • C25B15/08Supplying or removing reactants or electrolytes; Regeneration of electrolytes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention relates to a deuterium gas generator heavy water recovery device which comprises a diaphragm component, a three-dimensional metal screen plate, an upper metal clamping plate and a lower metal clamping plate which are connected with each other, wherein accommodating cavities and through holes communicated with the accommodating cavities are formed in the metal clamping plate and the lower metal clamping plate, and the diaphragm component and the three-dimensional metal screen plate are arranged in the accommodating cavities of the upper metal clamping plate and the lower metal clamping plate. The invention well prevents deuterium from mixing into an oxygen system by selecting the permeable and gas-barrier diaphragm, ensures that heavy water condensed from deuterium returns to a circulating system in time, and ensures that the function of the diaphragm is normally played by the support and the clamping of the metal powder sintering plate and the three-dimensional metal screen plate. Finally, the recovery of expensive heavy water materials is realized, and the production cost is greatly saved.

Description

Deuterium gas generator heavy water recovery device
Technical Field
The invention relates to a reflux device for recovering condensed heavy water in deuterium gas by a deuterium gas generator system, in particular to a heavy water recovery device for a deuterium gas generator.
Background
The existing heavy water electrolysis deuterium production equipment adopts a filter-pressing type structure, then a circulating pump is used for forcibly circulating electrolyte on an anode side and a cathode side to take away heat and bubbles generated by electrolysis, and the electrolytic cell structure is called as a double-circulation structure. In order to increase the purity of deuterium gas and reduce the influence of impurities in the electrolyte, an electrolytic cell structure has been developed in which the electrolyte is circulated only on the anode side by increasing the gas pressure on the cathode side, and this electrolytic cell structure is called a single-cycle structure. No matter single-cycle or double-cycle structure electrolytic cells, the gas electrolyzed from the electrolytic cells carries a large amount of heavy water vapor, and the heavy water vapor is condensed into heavy water after passing through a condenser. For the double-circulation structure, in order to avoid wasting expensive heavy water, only the heavy water condensed by the deuterium gas and oxygen condenser is required to flow back to respective phase separators; for the single-cycle structure, the deuterium pipeline cannot be connected to the oxygen-side phase separator in single-side cycle, so that the heavy water condensed from the deuterium is prevented from being wasted due to mixed explosion of the deuterium and the oxygen.
Disclosure of Invention
The deuterium generator heavy water recovery device can save cost, prevent expensive heavy water from being wasted, and not only can return heavy water condensed in deuterium gas to electrolyte at a circulating side, but also can prevent deuterium gas from being mixed into an oxygen side system.
The technical scheme provided by the invention for solving the technical problems is as follows: deuterium gas generator heavy water recovery unit, including diaphragm subassembly, three-dimensional metal mesh board and interconnect's last metal splint, lower metal splint, all be equipped with on metal splint, the lower metal splint and hold the chamber and with hold the communicating through-hole in chamber, diaphragm subassembly, three-dimensional metal mesh board are installed the intracavity is held to last metal splint, lower metal splint.
The diaphragm assembly comprises an upper diaphragm clamping plate, a lower diaphragm clamping plate and a water-permeable and gas-barrier diaphragm clamped between the upper diaphragm clamping plate and the lower diaphragm clamping plate.
The further technical scheme is that the upper diaphragm clamping plate and the lower diaphragm clamping plate are both alkali-resistant metal powder sintered plates.
The further technical scheme is that the porosity of the alkali-resistant metal powder sintered plate is 30-40%.
The further technical scheme is that the aperture ratio of the three-dimensional metal mesh plate is 60-80%.
The further technical scheme is that an O-shaped ring is arranged between the upper metal clamping plate and the lower metal clamping plate.
The invention has the following advantages: the invention well prevents deuterium from mixing into an oxygen system by selecting the permeable and gas-barrier diaphragm, ensures that heavy water condensed from deuterium returns to a circulating system in time, and ensures that the function of the diaphragm is normally played by the support and the clamping of the metal powder sintering plate and the three-dimensional metal screen plate. Finally, the recovery of expensive heavy water materials is realized, and the production cost is greatly saved.
Drawings
Fig. 1 is a schematic diagram of an explosive structure of the present invention.
Detailed Description
The present invention will be further described with reference to the following examples and the accompanying drawings.
As shown in fig. 1, the deuterium gas generator heavy water recovery device of the present invention comprises a diaphragm assembly, a three-dimensional metal mesh plate 5, and an upper metal splint 1 and a lower metal splint 2 which are connected with each other, wherein both the metal splint 1 and the lower metal splint 2 are provided with an accommodating cavity 3 and a through hole 4 communicated with the accommodating cavity 3, the diaphragm assembly and the three-dimensional metal mesh plate are installed in the accommodating cavity 3 of the upper metal splint 1 and the lower metal splint 2, and the diaphragm assembly comprises an upper diaphragm splint 6, a lower diaphragm splint 7, and a water and gas permeable and gas barrier diaphragm 8 sandwiched between the upper diaphragm splint 6 and the lower diaphragm splint 7.
In the embodiment, the invention selects the water-permeable gas-barrier diaphragm 8 with water-permeable and gas-barrier characteristics as the separation interface of deuterium and oxygen systems, and the deuterium gas transmission capacity is lower than 300cc/m2H/atm, heavy water permeability not less than 800g/m2/h/atm。
In this embodiment, the upper diaphragm clamping plate 6 and the lower diaphragm clamping plate 7 are both alkali-resistant metal powder sintered plates with a porosity of 30-40%. So that the support membrane remains flat and unfolded.
In this embodiment, the aperture ratio of the three-dimensional metal mesh plate is 60 to 80%; to keep the heavy water dispersed flowing.
As shown in fig. 1, in order to improve the sealing effect of the present embodiment, it is preferable that an O-ring 9 is provided between the upper metal clamping plate 1 and the lower metal clamping plate 2.
Although the present invention has been described with reference to the above embodiments, it should be understood that the present invention is not limited to the above embodiments, and those skilled in the art can make various changes and modifications without departing from the scope of the present invention.

Claims (6)

1. Deuterium gas generator heavy water recovery unit, its characterized in that includes diaphragm subassembly, three-dimensional metal otter board (5) and interconnect's last metal splint (1), lower metal splint (2), all be equipped with on metal splint (1), lower metal splint (2) and hold chamber (3) and with hold communicating through-hole (4) in chamber (3), diaphragm subassembly, three-dimensional metal otter board are installed in holding chamber (3) of last metal splint (1), lower metal splint (2).
2. Deuterium gas generator heavy water recovery device according to claim 1, characterized in that the membrane assembly comprises an upper membrane clamp plate (6), a lower membrane clamp plate (7) and a water and gas permeable barrier membrane (8) sandwiched between the upper and lower membrane clamp plates (6, 7).
3. Deuterium gas generator heavy water recovery device according to claim 2, characterized in that both the upper diaphragm clamping plate (6) and the lower diaphragm clamping plate (7) are alkali-resistant metal powder sintered plates.
4. Deuterium gas generator heavy water recovery device according to claim 3, characterized in that said alkali resistant metal powder sintered plate has a porosity of 30-40%.
5. The deuterium gas generator heavy water recovery device according to claim 1, wherein the aperture ratio of said solid metal mesh plate is 60-80%.
6. Deuterium gas generator heavy water recovery device according to claim 1, characterized in that an O-ring (9) is provided between the upper metal clamping plate (1) and the lower metal clamping plate (2).
CN202010828705.8A 2020-08-18 2020-08-18 Deuterium gas generator heavy water recovery device Pending CN111921345A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010828705.8A CN111921345A (en) 2020-08-18 2020-08-18 Deuterium gas generator heavy water recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010828705.8A CN111921345A (en) 2020-08-18 2020-08-18 Deuterium gas generator heavy water recovery device

Publications (1)

Publication Number Publication Date
CN111921345A true CN111921345A (en) 2020-11-13

Family

ID=73304362

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010828705.8A Pending CN111921345A (en) 2020-08-18 2020-08-18 Deuterium gas generator heavy water recovery device

Country Status (1)

Country Link
CN (1) CN111921345A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023026721A1 (en) * 2021-08-25 2023-03-02 大陽日酸株式会社 Deuterium recovery method and deuterium recovery equipment

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1107034A (en) * 1977-03-29 1981-08-18 Yuji Naruse Process for removing tritium from tritium-containing heavy water to recover tritium gas of high purity
CN202237447U (en) * 2011-07-20 2012-05-30 中国科学院广州地球化学研究所 Flat plate filter
CN105776438A (en) * 2016-02-04 2016-07-20 福建方明环保科技股份有限公司 Device and method for reducing content of deuterium in water
CN208250427U (en) * 2018-05-21 2018-12-18 江苏皇冠鸟生物科技股份有限公司 A kind of low deuterium-oxide production equipment
CN109680286A (en) * 2019-02-28 2019-04-26 王丽琴 A kind of device and method for producing deuterium
CN208893990U (en) * 2018-07-05 2019-05-24 王梁 A kind of device of semi-transparent bipolar membrane electrodialysis separation of deuterium

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1107034A (en) * 1977-03-29 1981-08-18 Yuji Naruse Process for removing tritium from tritium-containing heavy water to recover tritium gas of high purity
CN202237447U (en) * 2011-07-20 2012-05-30 中国科学院广州地球化学研究所 Flat plate filter
CN105776438A (en) * 2016-02-04 2016-07-20 福建方明环保科技股份有限公司 Device and method for reducing content of deuterium in water
CN208250427U (en) * 2018-05-21 2018-12-18 江苏皇冠鸟生物科技股份有限公司 A kind of low deuterium-oxide production equipment
CN208893990U (en) * 2018-07-05 2019-05-24 王梁 A kind of device of semi-transparent bipolar membrane electrodialysis separation of deuterium
CN109680286A (en) * 2019-02-28 2019-04-26 王丽琴 A kind of device and method for producing deuterium

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023026721A1 (en) * 2021-08-25 2023-03-02 大陽日酸株式会社 Deuterium recovery method and deuterium recovery equipment

Similar Documents

Publication Publication Date Title
EP0642601B1 (en) Dual-directional flow membrane support for water electrolyzers
AU2012312234B2 (en) High pressure gas system
CA2982973C (en) Diaphragm-electrode assembly for use in alkaline water electrolysers
CN111270256A (en) Movable water electrolysis hydrogen production hydrogenation device
WO2023093012A1 (en) Method for triple-electrode system electrolyzing water to produce hydrogen
CN111921345A (en) Deuterium gas generator heavy water recovery device
US10287692B2 (en) Diaphragm-electrode assembly for use in alkaline water electrolysers
KR101735766B1 (en) Oxygen and hydrogen gas feeder
JP2010216009A (en) Water electrolyzer
CN216550739U (en) Integrated pure water electrolyzer
RU2733726C2 (en) Electrolytic cell for producing hydrogen
FI20195758A1 (en) A system and a method for alkaline water electrolysis
KR20220057576A (en) Cross-flow water electrolysis
CN110556550A (en) Flow field plate and air-cooled electric pile
EP0157777A1 (en) Chemo-electric cell with at least one gas electrode
CN211170913U (en) Water tank and electrolytic bath integrated electrolytic device
CN115161676A (en) Device and method for directly producing hydrogen from seawater
CN212581571U (en) Electrolytic bath
CA3178248A1 (en) Electrolytic cell, method for operating a cell of this type and electrolyser
CN220376796U (en) End plate of water electrolyser
KR102032233B1 (en) An housing for a solid oxide fuel cell or solid oxide electrolysis cell
JP2011208163A (en) Water electrolyzer
CN219059140U (en) Polar plate of PEM water electrolytic bath
CN111118536A (en) Electrolysis chamber suitable for middle and edge air outlet and electrolysis bath thereof
CN218989354U (en) Device for extracting lithium from salt lake by electrochemical method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20201113