CN204122117U - Battery material reactor - Google Patents

Battery material reactor Download PDF

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Publication number
CN204122117U
CN204122117U CN201420589042.9U CN201420589042U CN204122117U CN 204122117 U CN204122117 U CN 204122117U CN 201420589042 U CN201420589042 U CN 201420589042U CN 204122117 U CN204122117 U CN 204122117U
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CN
China
Prior art keywords
reactor
entrance
communicated
feed arrangement
solid
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Expired - Lifetime
Application number
CN201420589042.9U
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Chinese (zh)
Inventor
柳俊
鲁生勇
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Liujun Technology Shanghai Co ltd
Original Assignee
JIANGSU MASITE NEW ENERGY TECHNOLOGY Co Ltd
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Priority to CN201420589042.9U priority Critical patent/CN204122117U/en
Application granted granted Critical
Publication of CN204122117U publication Critical patent/CN204122117U/en
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Abstract

The utility model discloses a kind of battery material reactor, comprise reactor, feed arrangement, feed arrangement for subsequent use, agitating device, metering device, constant-temperature water circulating device, PH adjusting device, drawing mechanism, Separation of Solid and Liquid clearing and drying device, checkout gear and hybrid packed device, the side of described reactor is provided with feed arrangement and feed arrangement for subsequent use, device agitating device on described reactor, metering device, constant-temperature water circulating device and PH adjusting device, the opposite side of described reactor is communicated with the entrance of drawing mechanism, the outlet of described drawing mechanism is communicated with the entrance of Separation of Solid and Liquid clearing and drying device, the described outlet of Separation of Solid and Liquid clearing and drying device is communicated with the entrance of checkout gear, the outlet of described checkout gear is communicated with the entrance of hybrid packed device.Reach material in course of reaction, form complete spheroidal cementite body, and crystalline solid degree of crystallinity is tight, without dephasign on X-ray diffraction figure, the object that peak is narrow in granularity.

Description

Battery material reactor
Technical field
The utility model relates to a kind of battery material reactor apparatus, particularly, relates to a kind of battery material reactor.
Background technology
At present, the liquid complexing in China's battery material industry and crystalline co-precipitate consersion unit are mainly by turbine type mixing plant, and this equipment meets the demand of domestic battery material substantially.But this kind of equipment makes degree of crystallinity defective tightness, cause little crystal seed excessive, cause the phenomenon that floccule mass crystalline polyimide is many simultaneously.Thus make its dephasign in X-ray diffraction too many, in size distribution, peak is compared wide.These phenomenons cause that battery cycle life is shorter the circulation more than 600 just can not occur battery droop; Decline fast with voltage platform.
Utility model content
The purpose of this utility model is, for the problems referred to above, proposes a kind of battery material reactor, to realize making material form the advantage of complete spheroidal cementite body in course of reaction.
For achieving the above object, the technical solution adopted in the utility model is:
A kind of battery material reactor, comprise reactor, feed arrangement, feed arrangement for subsequent use, agitating device, metering device, constant-temperature water circulating device, PH adjusting device, drawing mechanism, Separation of Solid and Liquid clearing and drying device, checkout gear and hybrid packed device, the side of described reactor is provided with feed arrangement and feed arrangement for subsequent use, device agitating device on described reactor, metering device, constant-temperature water circulating device and PH adjusting device, the opposite side of described reactor is communicated with the entrance of drawing mechanism, the outlet of described drawing mechanism is communicated with the entrance of Separation of Solid and Liquid clearing and drying device, the described outlet of Separation of Solid and Liquid clearing and drying device is communicated with the entrance of checkout gear, the outlet of described checkout gear is communicated with the entrance of hybrid packed device.
Further, described agitating device comprises shaft, stirring vane and stirring motor, and described stirring vane is arranged on shaft bottom, and described stirring motor is arranged on shaft top.
Further, described metering device is measuring pump.
The technical solution of the utility model has following beneficial effect:
The technical solution of the utility model, by arranging feed arrangement, feed arrangement for subsequent use, agitating device, metering device, constant-temperature water circulating device, PH adjusting device, drawing mechanism, Separation of Solid and Liquid clearing and drying device, checkout gear and hybrid packed device on reactor, this battery material reactor monolith structure is simple, each device coordinates accurate, thus reach material in course of reaction, form complete spheroidal cementite body, and crystalline solid degree of crystallinity is tight, without dephasign on X-ray diffraction figure, the object that peak is narrow in granularity.
Accompanying drawing explanation
Fig. 1 is the theory diagram of the battery material reactor described in the utility model embodiment;
Fig. 2 is the operational flowchart of the battery material reactor described in the utility model embodiment;
Fig. 3 a to Fig. 3 c is the structural representation of battery material reactor under different application described in the utility model embodiment.
By reference to the accompanying drawings, in the utility model embodiment, Reference numeral is as follows:
1-reactor; 2-shaft; 3-stirring vane; 4-stirring motor.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of battery material reactor, comprise reactor, feed arrangement, feed arrangement for subsequent use, agitating device, metering device, constant-temperature water circulating device, PH adjusting device, drawing mechanism, Separation of Solid and Liquid clearing and drying device, checkout gear and hybrid packed device, the side of reactor is provided with feed arrangement and feed arrangement for subsequent use, device agitating device on reactor, metering device, constant-temperature water circulating device and PH adjusting device, the opposite side of reactor is communicated with the entrance of drawing mechanism, the outlet of drawing mechanism is communicated with the entrance of Separation of Solid and Liquid clearing and drying device, the outlet of Separation of Solid and Liquid clearing and drying device is communicated with the entrance of checkout gear, the outlet of checkout gear is communicated with the entrance of hybrid packed device.
Wherein, agitating device comprises shaft 2, stirring vane 3 and stirring motor 4, and stirring vane 3 is arranged on shaft 2 bottom, and stirring motor 4 is arranged on shaft 2 top.
Metering device is measuring pump.
As shown in Figure 2, technical solutions of the utility model can be applied to the production of new energy materials (ni-mh, nickel-cadmium cell Material Field, field of lithium ion battery material), generate spherical particle material in the reactor.For the performance of battery material product, play decisive role.
Technical solutions of the utility model first drop into a certain proportion of pure water, ammoniacal liquor, NaOH in a kettle., then agitating device is opened, open measuring pump and input divalent metal solution, ammoniacal liquor, NaOH such as (nickel, cobalt, manganese) in proportion, 24 hours do not stop in injecting reactor, constant temperature system keeps uniform temperature constant, obtains spherical cathode battery material and opens discharge system and enter next workshop section, Separation of Solid and Liquid, cleaning, ageing, system carries out subsequent treatment, dry metering packing.
Wherein Fig. 3 a, Fig. 3 b, Fig. 3 c are respectively the design of different grain size, crystal controlling.The material of different performance can be produced, as the adjustment of the performances such as Large Copacity, high magnification, high-pressure solid.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although be described in detail the utility model with reference to previous embodiment, for a person skilled in the art, it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.

Claims (3)

1. a battery material reactor, it is characterized in that, comprise reactor, feed arrangement, feed arrangement for subsequent use, agitating device, metering device, constant-temperature water circulating device, PH adjusting device, drawing mechanism, Separation of Solid and Liquid clearing and drying device, checkout gear and hybrid packed device, the side of described reactor is provided with feed arrangement and feed arrangement for subsequent use, device agitating device on described reactor, metering device, constant-temperature water circulating device and PH adjusting device, the opposite side of described reactor is communicated with the entrance of drawing mechanism, the outlet of described drawing mechanism is communicated with the entrance of Separation of Solid and Liquid clearing and drying device, the described outlet of Separation of Solid and Liquid clearing and drying device is communicated with the entrance of checkout gear, the outlet of described checkout gear is communicated with the entrance of hybrid packed device.
2. battery material reactor according to claim 1, is characterized in that, described agitating device comprises shaft, stirring vane and stirring motor, and described stirring vane is arranged on shaft bottom, and described stirring motor is arranged on shaft top.
3. battery material reactor according to claim 1 and 2, is characterized in that, described metering device is measuring pump.
CN201420589042.9U 2014-10-13 2014-10-13 Battery material reactor Expired - Lifetime CN204122117U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420589042.9U CN204122117U (en) 2014-10-13 2014-10-13 Battery material reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420589042.9U CN204122117U (en) 2014-10-13 2014-10-13 Battery material reactor

Publications (1)

Publication Number Publication Date
CN204122117U true CN204122117U (en) 2015-01-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420589042.9U Expired - Lifetime CN204122117U (en) 2014-10-13 2014-10-13 Battery material reactor

Country Status (1)

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CN (1) CN204122117U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105561624A (en) * 2016-01-29 2016-05-11 太仓市微贯机电有限公司 Reactor equipment for spherical crystals
CN110194490A (en) * 2019-06-14 2019-09-03 长春工程学院 A kind of method and apparatus preparing magnetic nano ferroferric oxide
CN114130275A (en) * 2021-11-26 2022-03-04 广东长信精密设备有限公司 Cadmium chloride mixed crystal hydrate solution production system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105561624A (en) * 2016-01-29 2016-05-11 太仓市微贯机电有限公司 Reactor equipment for spherical crystals
CN110194490A (en) * 2019-06-14 2019-09-03 长春工程学院 A kind of method and apparatus preparing magnetic nano ferroferric oxide
CN114130275A (en) * 2021-11-26 2022-03-04 广东长信精密设备有限公司 Cadmium chloride mixed crystal hydrate solution production system
CN114130275B (en) * 2021-11-26 2024-03-26 广东长信精密设备有限公司 Cadmium chloride mixed crystal hydrate solution production system

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20210224

Address after: 201499 Building 1, 188 Xinghuo Road, Qingcun Town, Fengxian District, Shanghai

Patentee after: Liujun Technology (Shanghai) Co.,Ltd.

Address before: Room 418, area C, Xingye building, 97-1, Linghu Avenue, New District, Wuxi City, Jiangsu Province, 214135

Patentee before: JIANGSU MASITE NEW ENERGY TECHNOLOGY Co.,Ltd.

CX01 Expiry of patent term

Granted publication date: 20150128