CN201603555U - Precipitator - Google Patents

Precipitator Download PDF

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Publication number
CN201603555U
CN201603555U CN200920236814XU CN200920236814U CN201603555U CN 201603555 U CN201603555 U CN 201603555U CN 200920236814X U CN200920236814X U CN 200920236814XU CN 200920236814 U CN200920236814 U CN 200920236814U CN 201603555 U CN201603555 U CN 201603555U
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CN
China
Prior art keywords
baffle
stillpot
internal
ring
diameter
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 - Fee Related
Application number
CN200920236814XU
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Chinese (zh)
Inventor
张宗国
郝义田
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FOGANG JIATE METALS Co Ltd
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FOGANG JIATE METALS Co Ltd
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Priority to CN200920236814XU priority Critical patent/CN201603555U/en
Application granted granted Critical
Publication of CN201603555U publication Critical patent/CN201603555U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a precipitator, which comprises a precipitation tank, an injection pump. A ring-shaped baffle plate and a mixing device are arranged in the cavity of the precipitation tank; the ring-shaped baffle plate comprises an outer baffle plate and an inner baffle plate, meanwhile, the outer baffle plate is of a funnel structure, and the edge part of the upper end surface of the funnel structure is connected with the inner wall surface of the precipitation tank. The inner baffle plate is an inverted cone structure and is fixed inside the outer baffle plate. Paddles of the mixing device are arranged inside the inner baffle plate. The projection pump is provided with a mixing chamber and a first feeding port and a second feeding port which are communicated with the mixing chamber; the bottom end of the mixing chamber is provided with a flow guide pipe which extends to the upper end surface of the ring-shaped baffle plate in the precipitation tank. In the utility model, continuous cycling of materials in the precipitation tank can be realized, and the generation of coarse precipitate particles can be ensured.

Description

A kind of settling vessel
Technical field
The utility model relates to a kind of settling apparatus, relates in particular to a kind of continuous circulation floating bed settling vessel.
Background technology
Along with science and technology development, niobium is widely used in high-tech areas such as electronic ceramics, optical glass, artificial lens, superconductor, people begin to pay attention to the research of the various form products of niobium, and form industry, light glass, high-purity three other oxide product of level.In July, 1991, the Tokyo technology can be according to niobium oxide (Nb 2O 5) in the application of big capacity multi-layer ceramic capacitor, formulated Nb 2O 5Standard-required, it is 0.32 μ m that the particle mean size of rerum natura is required, and is used to make the fabulous electronic ceramics of dielectric properties.
Existing Nb 2O 5The mechanism of production technology is: H 2NbOF 5+ 5NH 3+ 4H 2O=Nb (OH) 5↓+5NH 4F; Its concrete technological process is: with fluooxycolumbic acid (H 2NbOF 5) solution squeezes in the settling vessel, feeds NH then in settling vessel 3, after stir the part, Nb (OH) 5With the floccule precipitation, its particle mean size is 60nm; Again with Nb (OH) 5Slurries filtration, and wash F-with pure water; To Nb (OH) 5Dry, after the roasting, mill sieves into final Nb at last 2O 5Product.
Existing Nb 2O 5The shortcoming of production technology and settling apparatus is: on technology along with NH 3Feeding, after acid-base neutralization, solution enter " metastable region ", produce supersaturated solution rapidly, a large amount of nucleus produce thereupon, have little time the growth and ageing; And, because the local stirring intensity of settling apparatus is big, there is not the condition of impelling and guarantee nuclei growth, the product of gained mostly is a flocky precipitate, granularity is meticulous, promptly enable the sediment that obtains reuniting, at roasting, mill sieve or make in the batch mixing process of ceramic capacitor and also can grind, when causing lead oxide-magnesium nitride-niobium oxide batch mixing " segregation "; The Nb of this coprecipitation mode gained 2O 5Be applied on the ceramic electronic, its dielectric constant is lower than 10000, can't make the fabulous electronic ceramics of dielectric properties.
The utility model content
The utility model embodiment provides a kind of settling vessel, can realize the circulation continuously in stillpot of oar material, guarantees the sedimentary generation of coarse granule.
The utility model embodiment provides a kind of settling vessel, be provided with ring-shaped baffle and agitating device in the chamber of described stillpot, described ring-shaped baffle is made of outer baffle and Internal baffle, described outer baffle is the funnel structure of both ends open, and the edge of its upper surface is connected on the internal face of described stillpot; Described Internal baffle is the back taper structure of both ends open, is fixed on the inside of described outer baffle; The blade of described agitating device places the inside of described Internal baffle;
Described jet pump is provided with mixing chamber, and first charging aperture that is connected with described mixing chamber, second charging aperture; The bottom of described mixing chamber is provided with mozzle, and described mozzle extends to the upper surface of the ring-shaped baffle in the described stillpot.
Wherein, described Internal baffle both ends open, the internal channel of formation institute ring-shaped baffle; The diameter of described Internal baffle upper surface is less than the diameter of described outer baffle upper surface, the diameter of described Internal baffle lower surface constitutes the outer tunnel of described ring-shaped baffle less than the diameter of described outer baffle lower surface between the outside wall surface of described Internal baffle and the internal face of described outer baffle.
The external diameter of described outer baffle upper surface equals the internal diameter of described stillpot cavity, and the edge of described outer baffle upper surface adopts welding or hinged mode to be connected on the internal face of described stillpot middle part; Described ring-shaped baffle is divided into two parts up and down with the inner chamber of described stillpot, and two-part liquid is connected by internal channel, the outer tunnel of described ring-shaped baffle up and down.
Described agitating device is by shaft, blade, inverted cone-shaped structure, and this device promptly has stirring action, and castering action is also arranged, and can abbreviate the pump impeller stirring system as; Described shaft vertically places on the central axis of described stillpot; Described blade is fixed on the described shaft, and described blade places the internal channel of described ring-shaped baffle.
Implement the utility model, have following beneficial effect:
The settling vessel that the utility model embodiment provides, jet pump can realize that giving of two kinds of materials mixed and the injection stillpot, be provided with ring-shaped baffle and agitating device in the stillpot, this ring-shaped baffle is made up of Internal baffle and outer baffle-plate, form inside and outside two passages, the blade of agitating device places the internal channel of ring-shaped baffle, when the blade rotary work, the oar material is circulation continuously on the inside and outside passage of ring-shaped baffle, guarantees the sedimentary generation of coarse granule.The utility model can be used for preparing the niobium oxide in coarse grain footpath, jet pump can realize that niobium liquid mixes with giving of ammonia, giving mixed oar material injects in the stillpot, the built-in pump impeller agitating device of stillpot has been realized the continuous circulation of oar material in groove, nucleus formation, grain growth have been guaranteed fully, the technical process of precipitation growth and ageing (slaking).The meta particle that is produced is thick, hard, do not wrap up mother liquor, absorption impurity is few, product purity is high, can satisfy the requirement of big capacity multi-layer ceramic capacitor.
Description of drawings
Fig. 1 is the structural representation of the settling vessel that provides of the utility model.
The specific embodiment
Below in conjunction with the accompanying drawing among the utility model embodiment, the technical scheme among the utility model embodiment is clearly and completely described.
Referring to Fig. 1, be the structural representation of the settling vessel that provides of the utility model, this settling vessel is made of stillpot 1 and jet pump 2.
Wherein, stillpot 1 is the round barrel shape cavity of sealing, and its upper end is provided with inlet valve 101 and air bleeding valve 102.
Jet pump 2 is provided with mixing chamber 201, and first charging aperture 202 that is connected with this mixing chamber 201 and second charging aperture 203; The bottom of mixing chamber 201 also is provided with mozzle 204, and this mozzle 204 passes the inlet valve 101 of stillpot 1, and extends in the cavity of stillpot 1.
Be provided with ring-shaped baffle 3 in the chamber of stillpot 1, the inlet valve 101 that the mozzle 204 of jet pump 2 passes stillpot 1 extends to the upper surface of ring-shaped baffle 3.This ring-shaped baffle 3 is made of outer baffle 301 and Internal baffle 302.Wherein, outer baffle 301 is the funnel structure of both ends open, and its top is inverted cone shape, and the bottom is a round barrel shape, and the diameter of its upper surface is greater than the diameter of lower surface; Internal baffle 302 is the back taper structure of both ends open, and the diameter of its upper surface is greater than the diameter of lower surface.Internal baffle 302 is fixed on the inside of outer baffle 301 by fixture, and stillpot cavity, outer baffle 301 and Internal baffle 302 are on the same central axis.
Internal baffle 302 both ends opens, the internal channel of formation ring-shaped baffle 3; The diameter of Internal baffle 302 upper surfaces is less than the diameter of outer baffle 301 upper surfaces, and the diameter of Internal baffle 302 lower surfaces forms the outer tunnel of ring-shaped baffle 3 less than the diameter of outer baffle 301 lower surfaces between the internal face of the outside wall surface of Internal baffle 302 and outer baffle 301.
The external diameter of outer baffle 301 upper surfaces equals the internal diameter of stillpot 1 cavity, and the edge of this upper surface adopts welding or hinged mode to be connected on the internal face of stillpot 1, and ring-shaped baffle 3 and stillpot 1 cavity are on the same central axis.Ring-shaped baffle 3 is divided into two parts up and down with the inner chamber of stillpot 1, and two-part liquid can be connected by the inside and outside passage on the ring-shaped baffle 3 up and down.
Further, stillpot also is provided with agitating device 4 in 1 chamber, and this agitating device 4 is made of shaft 401, blade 402, pump impeller.Shaft 401 is connected with described pump impeller, and shaft 401 vertically places on the central axis of stillpot 1; Blade 402 is fixed on the described shaft 401, and blade 402 places the internal channel of described ring-shaped baffle 3.The Internal baffle 302 common formations of this shaft 401, blade 402, back taper structure stir lifting device.Wherein, shaft 401 vertically places on the central axis of stillpot 1 cavity, and blade 402 is fixed on the shaft 401, and blade 402 places the inside of Internal baffle 302.
During concrete enforcement, the shaft 401 of agitating device 4 is connected with paddle 402, can be by the rotary speed of shaft 401 control blades 402.When blade 402 rotary works, slurry rises to the upper surface of Internal baffle 302 via the internal channel of ring-shaped baffle 3 from Internal baffle 302 lower surfaces; Via the outer tunnel of ring-shaped baffle 3, put the lower surface that end face drops to outer baffle 301 again, thereby realize the continuous circulation of slurry, guarantee the generation of deposit seed from outer baffle 301.
Optionally, in order to make slurry circulation continuously better in groove, during specific design, make the upper surface of a little higher than outer baffle 301 in upper surface of Internal baffle 302, the lower surface of Internal baffle 302 is higher than the lower surface of outer baffle 301.
As shown in Figure 1, the upper end of stillpot 1 is provided with air bleeding valve 102, is used for exhaust.The sidewall of stillpot 1 also is provided with mother liquor outlet valve 103, and this mother liquor outlet valve 103 is used to discharge mother liquor between the upper surface and lower surface of outer baffle 301.The bottom of stillpot 1 is provided with sediment outlet valve 104, is used to export the sediment in stillpot 1 chamber.
In the middle of concrete enforcement, the settling vessel that the utility model provides can be used for preparing coarse grained Nb 2O 5, its idiographic flow is as follows: with niobium liquid (H 2NbOF 5) injecting mixing chamber 201 from first charging aperture 202 of jet pump 2, second charging aperture 203 from jet pump 2 feeds ammonia (NH simultaneously 3).Because the suction function that the miscarriage of niobium liquid is given birth to can be brought ammonia in the mixing chamber 201 of jet pump 1, realize that niobium liquid mixes with giving of ammonia, and be injected into the upper surface of the ring-shaped baffle 3 in the stillpot 1 via the mozzle 204 of mixing chamber 201 bottoms.Because be provided with agitating device 4 in the chamber of stillpot 1, these agitating device 4 rotary works constantly will be expected the oar mixed lifting to liquid level, make the microcosmic mixing of liquid level charging place fine, can not produce local supersaturation.And set ring-shaped baffle 3 in stillpot 1 chamber, and the supporting with it agitating device with castering action 4 are realized slurry circulation continuously between the internal channel of ring-shaped baffle 3, outer tunnel.Agitating device 4 had both played the effect that mixes, and played again to promote the effect that realizes that the oar material circulates in stillpot, and the suspension that has molecule participates in circulation, and in a single day particle grows up, and just sinks to the bottom of stillpot 1, forms oarse-grained sediment.During concrete enforcement, the rotating speed that makes agitating device 4 blades is 60-80 rev/min, and rotating speed is low can not smashed deposit seed.And owing in the groove recycling precipitation reaction heat release (can reach 60 ℃), do not need outer heating just can well not realize deposit seed ageing (slaking) effect, resulting meta particle is thick, hard, do not wrap up mother liquor, adsorb that impurity is few, product purity is high.
The settling vessel that the utility model embodiment provides, jet pump can realize that giving of two kinds of materials mixed and the injection stillpot, be provided with ring-shaped baffle and agitating device in the stillpot, this ring-shaped baffle is made up of Internal baffle and interior plate washer, form inside and outside two passages, the blade of agitating device places the internal channel of ring-shaped baffle, when the blade rotary work, the oar material connects circulation on the inside and outside passage of ring-shaped baffle, guarantee the sedimentary generation of coarse granule.The utility model can be used for preparing the niobium oxide in coarse grain footpath, jet pump can realize that niobium liquid mixes with giving of ammonia, giving mixed oar material injects in the stillpot, the built-in pump impeller agitating device of stillpot has been realized the continuous circulation of oar material in groove, nucleus formation, grain growth have been guaranteed fully, the technical process of precipitation growth and ageing (slaking).The meta particle that is produced is thick, hard, do not wrap up mother liquor, absorption impurity is few, product purity is high, can satisfy the requirement of big capacity multi-layer ceramic capacitor.
The above is a preferred implementation of the present utility model; should be pointed out that for those skilled in the art, under the prerequisite that does not break away from the utility model principle; can also make some improvements and modifications, these improvements and modifications also are considered as protection domain of the present utility model.

Claims (10)

1. a settling vessel is characterized in that, comprising: stillpot, jet pump;
Be provided with ring-shaped baffle and agitating device in the chamber of described stillpot, described ring-shaped baffle is made of outer baffle and Internal baffle, and described outer baffle is a funnel structure, and the edge of its upper surface is connected on the internal face of described stillpot; Described Internal baffle is the back taper structure, is fixed on the inside of described outer baffle; The blade of described agitating device places the inside of described Internal baffle;
Described jet pump is provided with mixing chamber, and first charging aperture that is connected with described mixing chamber, second charging aperture; The bottom of described mixing chamber is provided with mozzle, and described mozzle extends to the upper surface of the ring-shaped baffle in the described stillpot.
2. settling vessel as claimed in claim 1 is characterized in that, described outer baffle is the funnel structure of both ends open, and its top is inverted cone shape, and the bottom is cylindric, and the diameter of upper surface is greater than the diameter of lower surface.
3. settling vessel as claimed in claim 2 is characterized in that, described Internal baffle is the back taper structure of both ends open, and the diameter of its upper surface constitutes the internal channel of described ring-shaped baffle greater than the diameter of lower surface.
4. settling vessel as claimed in claim 3, it is characterized in that, the diameter of described Internal baffle upper surface is less than the diameter of described outer baffle upper surface, the diameter of described Internal baffle lower surface constitutes the outer tunnel of described ring-shaped baffle less than the diameter of described outer baffle lower surface between the outside wall surface of described Internal baffle and the internal face of described outer baffle.
5. settling vessel as claimed in claim 4, it is characterized in that, the external diameter of described outer baffle upper surface equals the internal diameter of described stillpot cavity, and the edge of described outer baffle upper surface adopts welding or hinged mode to be connected on the internal face of described stillpot middle part; Described ring-shaped baffle is divided into two parts up and down with the inner chamber of described stillpot, and two-part liquid is connected by internal channel, the outer tunnel of described ring-shaped baffle up and down.
6. settling vessel as claimed in claim 5 is characterized in that, described stillpot cavity, outer baffle and Internal baffle are on the same central axis.
7. settling vessel as claimed in claim 6 is characterized in that described agitating device is made of shaft, blade, pump impeller; Described shaft is connected with described pump impeller, and described shaft vertically places on the central axis of described stillpot; Described blade is fixed on the described shaft, and described blade places the internal channel of described ring-shaped baffle.
8. as claim 1 or 7 described settling vessels, it is characterized in that the upper end of described stillpot is provided with inlet valve and air bleeding valve, the inlet valve that the mozzle of described jet pump passes described stillpot extends to the upper surface of ring-shaped baffle.
9. settling vessel as claimed in claim 8 is characterized in that the sidewall of described stillpot also is provided with the mother liquor outlet valve, and described mother liquor outlet valve is between the upper surface and lower surface of described outer baffle.
10. settling vessel as claimed in claim 9 is characterized in that the bottom of described stillpot also is provided with the sediment outlet valve.
CN200920236814XU 2009-09-30 2009-09-30 Precipitator Expired - Fee Related CN201603555U (en)

Priority Applications (1)

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CN200920236814XU CN201603555U (en) 2009-09-30 2009-09-30 Precipitator

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CN200920236814XU CN201603555U (en) 2009-09-30 2009-09-30 Precipitator

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102580658A (en) * 2012-03-21 2012-07-18 河北永泰柯瑞特化工有限公司 Stirring reaction kettle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102580658A (en) * 2012-03-21 2012-07-18 河北永泰柯瑞特化工有限公司 Stirring reaction kettle

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Guangdong Zhiyuan New Materials Co., Ltd.

Assignor: Fogang Jiate Metals Co., Ltd.

Contract record no.: 2011440000985

Denomination of utility model: Precipitation apparatus

Granted publication date: 20101013

License type: Exclusive License

Record date: 20110905

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20101013

Termination date: 20130930