CN204388487U - Pole plate dryer - Google Patents

Pole plate dryer Download PDF

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Publication number
CN204388487U
CN204388487U CN201420861235.5U CN201420861235U CN204388487U CN 204388487 U CN204388487 U CN 204388487U CN 201420861235 U CN201420861235 U CN 201420861235U CN 204388487 U CN204388487 U CN 204388487U
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CN
China
Prior art keywords
pole plate
gas
nitrogen
chamber
oxygen
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
CN201420861235.5U
Other languages
Chinese (zh)
Inventor
陈禹
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.)
Yunnan Sun-Stone Energy Science And Technology Industrial Co Ltd
Original Assignee
Yunnan Sun-Stone Energy Science And Technology Industrial 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 Yunnan Sun-Stone Energy Science And Technology Industrial Co Ltd filed Critical Yunnan Sun-Stone Energy Science And Technology Industrial Co Ltd
Priority to CN201420861235.5U priority Critical patent/CN204388487U/en
Application granted granted Critical
Publication of CN204388487U publication Critical patent/CN204388487U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • 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
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The utility model relates to and a kind ofly carries out dry pole plate dryer to the pole plate after changing into, and the nitrogen can isolated in air carries out drying to pole plate.The gas-heated room comprising hothouse and be communicated with it, also comprises the deaerating chamber being provided with gas separation membrane; Yang Dan separation chamber is isolated into nitrogen chamber and oxygen room by institute's gas separation membrane; Described nitrogen chamber is connected with air compressor by air inlet pipe; Described nitrogen chamber is communicated with described gas-heated room by downtake pipe; Magnetic valve is provided with in described downtake pipe; Be provided with oxygen sensor in described nitrogen chamber, described oxygen sensor is electrically connected with Programmable Logic Controller, and described Programmable Logic Controller and described magnetic valve are electrically connected.By gas separation membrane, isolate concentration nitrogen up to standard and drying is carried out to pole plate, avoid pole plate to be oxidized in dry run, can not only be cost-saving, obtained nitrogen and oxygen can also produce economic benefit, and do not have disposal of pollutants, meet environmental requirement.

Description

Pole plate dryer
Technical field
The utility model relates to and a kind ofly carries out dry pole plate dryer to the pole plate after changing into.
Background technology
Green plate is after changing into, and form the pole plate with active material, active material is easily oxidized, and therefore, current pole plate dryer adopts the inert gas of high temperature to carry out drying to pole plate.The source of inert gas is be purchased from air feed to buy mostly, this adds increased production cost.The main component of air is nitrogen and oxygen, and nitrogen is a kind of noiseless tasteless nontoxic, and the inactive gas of chemical property, need when HTHP even adds catalyst could with other substance reactions.Employing air separating method obtains the selection that nitrogen is undoubtedly a kind of cheap and simple, the technology of membrane separation process to be exactly a kind of with air be waste nitrogen: under pressure, utilize oxygen and nitrogen in gas separation membrane different permeability to make oxygen and nitrogen separation.
Utility model content
The purpose of this utility model is to provide a kind of pole plate dryer, and the nitrogen can isolated in air carries out drying to pole plate.
For achieving the above object, the technical scheme that the utility model adopts is: a kind of pole plate dryer, and the gas-heated room comprising hothouse and be communicated with it, also comprises the deaerating chamber being provided with gas separation membrane; Yang Dan separation chamber is isolated into nitrogen chamber and oxygen room by institute's gas separation membrane; Described nitrogen chamber is connected with air compressor by air inlet pipe; Described nitrogen chamber is communicated with described gas-heated room by downtake pipe; Magnetic valve is provided with in described downtake pipe; Be provided with oxygen sensor in described nitrogen chamber, described oxygen sensor is electrically connected with Programmable Logic Controller, and described Programmable Logic Controller and described magnetic valve are electrically connected.
Preferably, the path of described air inlet pipe is provided with air cleaner.Air cleaner can filter out moisture content, fluid, dust and other impurity in air, can improve the quality of nitrogen.
Preferably, the path of described downtake pipe is removably connected with deoxidation pipe, in described deoxidation pipe, is filled with deoxidier.Deoxidier can remove oxygen further, reduces oxygen content.
Preferably, described oxygen room is connected with gas bottle by second exhaust pipe.Gas bottle, for collecting the oxygen separated, in order to his use, avoids waste.
Preferably, described gas-heated room is arranged on the below of described hothouse, and described gas-heated indoor are provided with electric heater.Gas-heated room is arranged on below hothouse, high-temperature hot air-flow so after heating just can naturally rise in hothouse, and the cold airflow after cooling drops to gas-heated indoor again, so just achieves circulating-heating, not only the thermal efficiency is high, can also saving gas.
The utility model has following beneficial effect: compressor, by the nitrogen chamber sent into after air compressing in deaerating chamber, because gas separation membrane is easy to through oxygen, is not easy to through nitrogen, therefore, nitrogen is trapped within nitrogen chamber, and oxygen passes through from gas separation membrane, enrichment in oxygen room; Oxygen sensor detects the oxygen concentration of nitrogen chamber, and send signal to Programmable Logic Controller, when oxygen concentration is reduced to standard-required, Programmable Logic Controller just Controlling solenoid valve opens valve, gas in nitrogen chamber just enters into gas-heated indoor from downtake pipe, after concentration nitrogen up to standard is heated, drying is carried out to the pole plate in hothouse, prevent pole plate oxidized in dry run.Can not only be cost-saving, obtained nitrogen and oxygen can also produce economic benefit, and do not have disposal of pollutants, meet environmental requirement.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
As shown in Figure 1, a kind of pole plate dryer, gas-heated 2 Room comprising hothouse 1 and be communicated with it, also comprises the deaerating chamber being provided with gas separation membrane 3; Deaerating chamber is isolated into nitrogen chamber and oxygen room by institute's gas separation membrane 3; Described nitrogen chamber is connected with air compressor 11 by air inlet pipe 9; Described nitrogen chamber is communicated with described gas-heated room 2 by downtake pipe 8; Magnetic valve 6 is provided with in described downtake pipe 8; Be provided with oxygen sensor 4 in described nitrogen chamber, described oxygen sensor 4 is electrically connected with Programmable Logic Controller 5, and described Programmable Logic Controller 5 is electrically connected with described magnetic valve 6.
In technique scheme, compressor 11 by the nitrogen chamber sent into after air compressing in deaerating chamber, because gas separation membrane 3 is easy to through oxygen, be not easy to through nitrogen, therefore, nitrogen is trapped within nitrogen chamber, oxygen passes through from gas separation membrane 3, enrichment in oxygen room; Oxygen sensor 4 detects the oxygen concentration of nitrogen chamber, and send signal to Programmable Logic Controller 5, when oxygen concentration is reduced to standard-required, Programmable Logic Controller 5 just Controlling solenoid valve 6 is opened, gas in nitrogen chamber just enters into gas-heated indoor from downtake pipe 8, after concentration nitrogen up to standard is heated, drying is carried out to the pole plate in hothouse 1, prevent pole plate oxidized in dry run.Can not only be cost-saving, obtained nitrogen and oxygen can also produce economic benefit, and do not have disposal of pollutants, meet environmental requirement.
Preferably, the path of described air inlet pipe 9 is provided with air cleaner 10.Air cleaner can filter out moisture content, fluid, dust and other impurity in air, can improve the quality of nitrogen.
Preferably, the path of described downtake pipe 8 is removably connected with deoxidation pipe 7, in described deoxidation pipe 7, is filled with deoxidier.Deoxidier can remove oxygen further, reduces oxygen content.
Preferably, described oxygen room is connected with gas bottle 13 by second row 12 tracheae.Gas bottle 13, for collecting the oxygen separated, in order to his use, avoids waste.
Preferably, described gas-heated room 2 is arranged on the below of described hothouse 1, is provided with electric heater in described gas-heated room 2.Gas-heated room 2 is arranged on below hothouse 1, high-temperature hot air-flow so after heating just can naturally rise in hothouse 1, and the cold airflow after cooling drops in gas-heated room 2 again, so just achieves circulating-heating, not only the thermal efficiency is high, can also saving gas.

Claims (5)

1. a pole plate dryer, the gas-heated room comprising hothouse and be communicated with it, is characterized in that: also comprise the deaerating chamber being provided with gas separation membrane; Yang Dan separation chamber is isolated into nitrogen chamber and oxygen room by institute's gas separation membrane; Described nitrogen chamber is connected with air compressor by air inlet pipe; Described nitrogen chamber is communicated with described gas-heated room by downtake pipe; Magnetic valve is provided with in described downtake pipe; Be provided with oxygen sensor in described nitrogen chamber, described oxygen sensor is electrically connected with Programmable Logic Controller, and described Programmable Logic Controller and described magnetic valve are electrically connected.
2. pole plate dryer according to claim 1, is characterized in that: the path of described air inlet pipe is provided with air cleaner.
3. pole plate dryer according to claim 1, is characterized in that: the path of described downtake pipe is removably connected with deoxidation pipe, is filled with deoxidier in described deoxidation pipe.
4. pole plate dryer according to claim 1, is characterized in that: described oxygen room is connected with gas bottle by second exhaust pipe.
5. pole plate dryer according to claim 1, is characterized in that: described gas-heated room is arranged on the below of described hothouse, and described gas-heated indoor are provided with electric heater.
CN201420861235.5U 2014-12-31 2014-12-31 Pole plate dryer Expired - Fee Related CN204388487U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420861235.5U CN204388487U (en) 2014-12-31 2014-12-31 Pole plate dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420861235.5U CN204388487U (en) 2014-12-31 2014-12-31 Pole plate dryer

Publications (1)

Publication Number Publication Date
CN204388487U true CN204388487U (en) 2015-06-10

Family

ID=53361201

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420861235.5U Expired - Fee Related CN204388487U (en) 2014-12-31 2014-12-31 Pole plate dryer

Country Status (1)

Country Link
CN (1) CN204388487U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114788974A (en) * 2022-04-07 2022-07-26 坤育环境发展(云南)有限公司 Low-oxygen sulfur-free drying method and device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114788974A (en) * 2022-04-07 2022-07-26 坤育环境发展(云南)有限公司 Low-oxygen sulfur-free drying method and device
CN114788974B (en) * 2022-04-07 2024-03-22 坤育环境发展(云南)有限公司 Method and device for low-oxygen sulfur-free drying

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150610

Termination date: 20191231