CN203663718U - Novel continuous dissolver - Google Patents

Novel continuous dissolver Download PDF

Info

Publication number
CN203663718U
CN203663718U CN201320807770.8U CN201320807770U CN203663718U CN 203663718 U CN203663718 U CN 203663718U CN 201320807770 U CN201320807770 U CN 201320807770U CN 203663718 U CN203663718 U CN 203663718U
Authority
CN
China
Prior art keywords
cylindrical shell
reaction zone
lower reaction
rong district
rong
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.)
Expired - Lifetime
Application number
CN201320807770.8U
Other languages
Chinese (zh)
Inventor
张天祥
杨宝光
吴伟
于红箭
刘建鹏
柴世全
李雄
王朝阳
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.)
4O4 Co Ltd CHINA NATIONAL NUCLEAR Corp
Original Assignee
4O4 Co Ltd CHINA NATIONAL NUCLEAR Corp
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 4O4 Co Ltd CHINA NATIONAL NUCLEAR Corp filed Critical 4O4 Co Ltd CHINA NATIONAL NUCLEAR Corp
Priority to CN201320807770.8U priority Critical patent/CN203663718U/en
Application granted granted Critical
Publication of CN203663718U publication Critical patent/CN203663718U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The utility model belongs to the technical field of uranium purification technology, particularly relates to a novel continuous dissolver and provides a U3O8 continuous and stable dissolver capable of being used for the nuclear fuel to cycle raw materials of natural uranium purification. The continuous dissolver comprises a lower reaction zone cylinder body (1), an upper continuous dissolving zone cylinder body (2), a discharge port (10), an empting port (11), a liquid level meter, a flower plate and filter screen (14) and electrical heating devices (15), wherein the lower reaction zone cylinder body (1) adopts a combined body of a cylindrical cylinder body and conical lower part; the electrical heating devices (15) are arranged on the outer sides of the lower reaction zone cylinder body (1); the empting port (11) is arranged at the lower end of the lower reaction zone cylinder body (1); the upper continuous dissolving zone cylinder body (2) adopts a cylindrical structure; the discharge port (10) is formed in the lower end of the upper continuous dissolving area cylinder body (2); the lower end of the liquid level meter is connected with the empting port (11); the lower reaction zone cylinder body (1) is connected with the upper continuous dissolving zone cylinder body (2) through flanges and screw nuts; the fixed flower plate and filter screen (14) is arranged between the lower reaction zone cylinder body and the upper continuous dissolving zone cylinder body.

Description

A kind of new type of continuous dissolvers
Technical field
The invention belongs to uranium purifying process technology technical field, be specifically related to a kind of new type of continuous dissolvers.
Background technology
Uranium purifying process mainly comprises U 3o 8the operations such as dissolving, abstraction purification, inspissation denitration, hydration reduction and vent gas treatment.At present, U 3o 8dissolution mechanism mainly contains batch (-type) and dissolves and continuous-dissolution.U at present 3o 8dissolution process mainly takes batch (-type) to dissolve, and its main equipment is pot type batch dissolver, and it is simple in structure, and reinforced and discharging and deslagging ratio are easier to realize, and does not exist to start and stop and occur dissolving the problems such as feed liquid is defective.But its equipment volume is larger, and automaticity is lower, and the feed liquid composition producing differs greatly, and brought certain impact to subsequent handling continuous and steady operation.
Continuous-dissolution has that equipment occupation space is little, labor intensity of operating staff is low and the composition of lysate is comparatively constant, exhaust velocity stable higher without gas peak, efficiency, be easy to control, can realize the advantages such as system continuous and steady operation.But also do not carry out performance study and industrial Enlargement Design for the key equipment dissolvers of dissolution process at present, in order to improve the integrated artistic technical merit of planning to build uranium purifying conversion production line, need a kind of dissolved efficiency of exploratory development badly high, and there is the U of good operation stability 3o 8dissolvers.
The utility model, in conjunction with continuous-dissolution technique, continuous-dissolution device finding, bases oneself upon existing achievement in research and has carried out U 3o 8design, development and the continuous-dissolution experimental study project of continuous-dissolution device, set up continuous-dissolution process system, carries out U 3o 8continuous-dissolution test.
Summary of the invention
The object of the invention is, for prior art deficiency, provide a kind of U 3o 8can be used for continuous, the stabilizing dissolved device of nuclear fuel cycle natural uranium purified feed stock.
Technical scheme of the present invention is:
A kind of new type of continuous dissolvers, comprise lower reaction zone cylindrical shell, Ji Rong district, top cylindrical shell, discharging opening, turned letter mouth, liquid level gauge, card and screen pack and electric heater unit, described lower reaction zone cylindrical shell is the combination of cylinder stack shell and cone lower curtate, and its outside is provided with electric heater unit; Described turned letter mouth is located at cylindrical shell lower end, lower reaction zone; Described Ji Rong district, top cylindrical shell is cylindrical structure, and its lower end is provided with discharging opening; Described liquid level gauge lower end is connected with turned letter mouthful; Between lower reaction zone cylindrical shell and Ji Rong district, top cylindrical shell, be connected by flange, nut, in the middle of two cylindrical shells, be provided with fixing card and screen pack.
Described lower reaction zone cylindrical shell comprises reaction zone inner core and cooling endless tube, lower reaction zone cylindrical shell and reaction zone inner core bottom welding, cooling endless tube is fixed on the fixed support device of lower reaction zone inner barrel, and its entrance end passes lower reaction zone cylinder lateral wall and seals with lower reaction zone barrel soldering.
Described Ji Rong district, top cylindrical shell comprises Ji Rong district inner core, tail gas outlet, presses the empty empty endless tube that stirs of entrance, solid material feed pipe, solvent feed pipe and pressure that stirs, in described Ji Rong district cylindrical shell, Ji Rong district inner core is installed, Ji Rong district inner core and card and screen pack welding, cylindrical shell upper end, Ji Rong district, top has tail gas outlet; Solid material feed pipe upper end is welded on cylindrical shell top, Ji Rong district, top and has feeding-in solid body mouth through cylindrical shell upper end, Ji Rong district, top, and its pipe shaft runs through lower reaction zone cylindrical shell, top Ji Rong district cylindrical shell and card and screen pack inserts in reaction zone inner core; Solvent feed pipe upper end is welded on cylindrical shell top, Ji Rong district, top and has solvent feed mouth through cylindrical shell upper end, Ji Rong district, top, and its pipe shaft runs through lower reaction zone cylindrical shell, top Ji Rong district cylindrical shell and card and screen pack inserts in reaction zone inner core; Press the empty endless tube upper end of stirring be welded on cylindrical shell top, Ji Rong district, top and have and press the empty entrance that stirs through cylindrical shell upper end, Ji Rong district, top, its pipe shaft runs through lower reaction zone cylindrical shell, top Ji Rong district cylindrical shell and card and screen pack is around in reaction zone inner core outside circlewise.
The invention has the beneficial effects as follows:
1. at conversion zone, inner core is set, and the empty stirring of pressure is set in bottom, impel feed liquid at reaction zone baffling, increase stroke;
2. in upper cavity, inner core is set, with conversion zone junction, demister is not set, make the inner potential difference that forms of dissolvers, realize smooth and easy discharging;
3.U 3o 8solid, solubilising reagent all adopt bottom feed, have avoided material to go out dissolver with air-flow carrier band, have reduced the loss of material.
Accompanying drawing explanation
Fig. 1 is continuous-dissolution device structural representation;
In figure: 1. lower reaction zone cylindrical shell; 2. top Ji Rong district cylindrical shell; 3. reaction zone inner core; 4.Ji Rong district inner core; 5. tail gas outlet; 6. press the empty entrance that stirs; 7. solid material import; 8. solvent inlet; 9. press the empty endless tube that stirs; 10. discharging opening; 11. turned letters mouthful; 12. liquid level gauges; 13. cooling endless tubes; 14. cards and screen pack; 15. electric heater units.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment, the processing method of a kind of multiple tracks spectral measurement to the present invention's proposition is further introduced:
A kind of new type of continuous dissolvers, comprise lower reaction zone cylindrical shell 1, Ji Rong district, top cylindrical shell 2, discharging opening 10, turned letter mouth 11, liquid level gauge 12, card and screen pack 14 and electric heater unit 15, described lower reaction zone cylindrical shell 1 is the combination of cylinder stack shell and cone lower curtate, and its outside is provided with electric heater unit 15; Described turned letter mouth 11 is located at lower reaction zone cylindrical shell 1 lower end; Described Ji Rong district, top cylindrical shell 2 is cylindrical structure, and its lower end is provided with discharging opening 10; Described liquid level gauge 12 lower ends are connected with turned letter mouth 11; Between lower reaction zone cylindrical shell 1 and Ji Rong district, top cylindrical shell 2, be connected by flange, nut, in the middle of two cylindrical shells, be provided with fixing card and screen pack 14.
Described lower reaction zone cylindrical shell 1 comprises reaction zone inner core 3 and cooling endless tube 13, lower reaction zone cylindrical shell 1 and reaction zone inner core 3 bottom weldings, cooling endless tube 13 is fixed on the fixed support device of lower reaction zone cylindrical shell 1 inside, its entrance end through lower reaction zone cylindrical shell 1 sidewall and with lower reaction zone cylindrical shell 1 welded seal.
Described Ji Rong district, top cylindrical shell 2 comprises Ji Rong district inner core 4, tail gas outlet 5, presses the empty empty endless tube 9 that stirs of entrance 6, solid material feed pipe 7, solvent feed pipe 8 and pressure that stirs, in described Ji Rong district cylindrical shell 2, Ji Rong district inner core 4 is installed, Ji Rong district inner core 4 welds with card and screen pack 14, and cylindrical shell 2 upper ends, Ji Rong district, top have tail gas outlet 5; Solid material feed pipe 7 upper ends are welded on cylindrical shell 2 tops, Ji Rong district, top and have feeding-in solid body mouth through cylindrical shell 2 upper ends, Ji Rong district, top, and its pipe shaft runs through lower reaction zone cylindrical shell 1, Ji Rong district, top cylindrical shell 2 and card and screen pack 14 inserts in reaction zone inner core 3; Solvent feed pipe 8 upper ends are welded on cylindrical shell 2 tops, Ji Rong district, top and have solvent feed mouth through cylindrical shell 2 upper ends, Ji Rong district, top, and its pipe shaft runs through lower reaction zone cylindrical shell 1, Ji Rong district, top cylindrical shell 2 and card and screen pack 14 inserts in reaction zone inner core 3; Press empty endless tube 9 upper ends of stirring be welded on cylindrical shell 2 tops, Ji Rong district, top and have and press the empty entrance 6 that stirs through cylindrical shell 2 upper ends, Ji Rong district, top, its pipe shaft runs through lower reaction zone cylindrical shell 1, Ji Rong district, top cylindrical shell 2 and card and screen pack 14 is around in reaction zone inner core 3 outsides circlewise.
Dissolvers overall structure is cylinder, point upper and lower two parts.Bottom is main reaction region, its inside arranges inner core, solid material contacts in inner core with dissolving acid and reacts, react incomplete pressed powder and overflow from inner core top with lysate, under the effect of density contrast and gravity, flow downward, after empty stirring pressed in bottom, following feed liquid turns back again upwards mobile, pressed powder is followed feed liquid and just in dissolvers conversion zone, is formed baffling like this, and has increased the stroke of feed liquid, makes solid-liquid two-phase abundant haptoreaction in lower reaction zone.
Dissolvers middle part arranges screen pack, is to take and remove the mist of carrying secretly in tail gas out of with lysate for fear of pressed powder.In dissolvers outer setting, from siding temperaturing heating belt, inside arranges cooling coil effectively to control solubilizing reaction temperature.Dissolvers upper cavity arranges inner core and is directly connected with lower conversion zone, makes discharging smooth and easy to ensure enough potential differences.The uranyl nitrate solution generating like this can overcome the resistance that feed liquid forms by filter screen and fall under potential difference effect, flows out through middle part overflow pipe.

Claims (3)

1. a new type of continuous dissolvers, it is characterized in that: comprise lower reaction zone cylindrical shell (1), Ji Rong district, top cylindrical shell (2), discharging opening (10), turned letter mouthful (11), liquid level gauge (12), card and screen pack (14) and electric heater unit (15), described lower reaction zone cylindrical shell (1) is the combination of cylinder stack shell and cone lower curtate, and its outside is provided with electric heater unit (15); Described turned letter mouthful (11) is located at lower reaction zone cylindrical shell (1) lower end; Described Ji Rong district, top cylindrical shell (2) is cylindrical structure, and its lower end is provided with discharging opening (10); Described liquid level gauge (12) lower end is connected with turned letter mouthful (11); Between lower reaction zone cylindrical shell (1) and Ji Rong district, top cylindrical shell (2), be connected by flange, nut, in the middle of two cylindrical shells, be provided with fixing card and screen pack (14).
2. a kind of new type of continuous dissolvers as claimed in claim 1, it is characterized in that: described lower reaction zone cylindrical shell (1) comprises reaction zone inner core (3) and cooling endless tube (13), lower reaction zone cylindrical shell (1) and reaction zone inner core (3) bottom welding, cooling endless tube (13) is fixed on the inner fixed support device of lower reaction zone cylindrical shell (1), its entrance end through lower reaction zone cylindrical shell (1) sidewall and with lower reaction zone cylindrical shell (1) welded seal.
3. a kind of new type of continuous dissolvers as claimed in claim 1, it is characterized in that: described Ji Rong district, top cylindrical shell (2) comprises Ji Rong district inner core (4), tail gas outlet (5), presses the empty empty endless tube (9) that stirs of entrance (6), solid material feed pipe (7), solvent feed pipe (8) and pressure that stirs, Ji Rong district inner core (4) is installed in described Ji Rong district cylindrical shell (2), Ji Rong district inner core (4) and card and screen pack (14) welding, Ji Rong district, top cylindrical shell (2) upper end has tail gas outlet (5); Solid material feed pipe (7) upper end is welded on Ji Rong district, top cylindrical shell (2) top and has feeding-in solid body mouth through Ji Rong district, top cylindrical shell (2) upper end, and its pipe shaft runs through lower reaction zone cylindrical shell (1), Ji Rong district, top cylindrical shell (2) and card and screen pack (14) inserts in reaction zone inner core (3); Solvent feed pipe (8) upper end is welded on Ji Rong district, top cylindrical shell (2) top and has solvent feed mouth through Ji Rong district, top cylindrical shell (2) upper end, and its pipe shaft runs through lower reaction zone cylindrical shell (1), Ji Rong district, top cylindrical shell (2) and card and screen pack (14) inserts in reaction zone inner core (3); Press empty endless tube (9) upper end of stirring be welded on Ji Rong district, top cylindrical shell (2) top and have and press the empty entrance (6) that stirs through Ji Rong district, top cylindrical shell (2) upper end, its pipe shaft runs through lower reaction zone cylindrical shell (1), Ji Rong district, top cylindrical shell (2) and card and screen pack (14) is around in reaction zone inner core (3) outside circlewise.
CN201320807770.8U 2013-12-10 2013-12-10 Novel continuous dissolver Expired - Lifetime CN203663718U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320807770.8U CN203663718U (en) 2013-12-10 2013-12-10 Novel continuous dissolver

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320807770.8U CN203663718U (en) 2013-12-10 2013-12-10 Novel continuous dissolver

Publications (1)

Publication Number Publication Date
CN203663718U true CN203663718U (en) 2014-06-25

Family

ID=50960053

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320807770.8U Expired - Lifetime CN203663718U (en) 2013-12-10 2013-12-10 Novel continuous dissolver

Country Status (1)

Country Link
CN (1) CN203663718U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104143365A (en) * 2014-07-08 2014-11-12 中国核电工程有限公司 Neutron poison sandwich structure with openings in continuous dissolver
CN105895176A (en) * 2015-01-01 2016-08-24 杨宝光 Spent fuel element segment consistency dissolver provided with spiral pushing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104143365A (en) * 2014-07-08 2014-11-12 中国核电工程有限公司 Neutron poison sandwich structure with openings in continuous dissolver
CN105895176A (en) * 2015-01-01 2016-08-24 杨宝光 Spent fuel element segment consistency dissolver provided with spiral pushing device
CN105895176B (en) * 2015-01-01 2018-07-17 杨宝光 A kind of spent fuel element section continuous-dissolution device with spiral-push device

Similar Documents

Publication Publication Date Title
CN202924730U (en) Inner floating ball type sulfur sealing tank
CN104328291B (en) A kind of oxidation price modification equipment Pu (III) being oxidizing to Pu (IV)
CN203663718U (en) Novel continuous dissolver
CN104789782A (en) BP price-adjusting, degassing and acid-adjusting integrated device and method in Purex process
CN107051239A (en) A kind of automobile urea liquid field production device
CN107369486A (en) The regulation of 2AF and OF feed liquids prepares integrated system in a kind of aftertreatment technology flow
CN205517515U (en) Urea solution dosing unit of pneumatic stirring
CN104332210A (en) Apparatus for removing nitrous acid in reprocessing feed solution
CN102350090A (en) Device for continuously extracting Chinese medicine
CN208856974U (en) It is a kind of for handling the overcritical water oxidization reactor of high concentrated organic waste liquid
CN202263417U (en) Apparatus for continuous extraction of traditional Chinese medicine
CN204724166U (en) Air blast chemical combination bucket in electrolytic manganese process
CN204570004U (en) Purex flow BP price modification, degassed, acid adjustment integrated apparatus
CN204544091U (en) The vertical Agitation Tank of a kind of pharmacy
CN204404862U (en) Material heat exchanger in a kind of Treatment of Sludge
CN203235409U (en) Device for collecting and treating waste gas in fluorescent powder waste treatment process
CN205235942U (en) Gas -liquid reaction device
CN203448097U (en) Nitration reaction kettle
CN207877293U (en) Resin waste liquid recovery apparatus
CN203436854U (en) Ultrasonic-assisted supercritical fluid extraction device for gutta percha
CN202376962U (en) Head tank
CN204246850U (en) A kind of paraffin oil and the accurate separation system device of carrene
CN204204437U (en) A kind of equipment removing nitrous acid in aftertreatment feed liquid
CN202609944U (en) Neutralization concentration device for ammonium phosphate production
CN203610133U (en) Novel furfural hydrogenation reactor

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20140625

CX01 Expiry of patent term