CN202492587U - Fluorite-preparing carbon anode mechanism - Google Patents

Fluorite-preparing carbon anode mechanism Download PDF

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Publication number
CN202492587U
CN202492587U CN201220070442XU CN201220070442U CN202492587U CN 202492587 U CN202492587 U CN 202492587U CN 201220070442X U CN201220070442X U CN 201220070442XU CN 201220070442 U CN201220070442 U CN 201220070442U CN 202492587 U CN202492587 U CN 202492587U
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CN
China
Prior art keywords
carbon anode
fluorite
utility
carbon
groove
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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
CN201220070442XU
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Chinese (zh)
Inventor
路建顺
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.)
LINZHOU YUTONG CARBON CO Ltd
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LINZHOU YUTONG CARBON CO Ltd
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Priority to CN201220070442XU priority Critical patent/CN202492587U/en
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Publication of CN202492587U publication Critical patent/CN202492587U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model belongs to the field of fluorite preparation, and relates to a fluorite-preparing carbon anode mechanism. The fluorite-preparing carbon anode mechanism comprises a carbon anode plate, wherein an axial groove is arranged on the surface of the carbon anode plate. According to the utility model, the groove is arranged on the carbon anode plate, the largest possible superficial area of the carbon anode inside a limited fluorite-preparing tank is solved; improvement of the quality is facilitated under the condition of the original equipment; the cost is reduced; the polarization is reduced, and the prolonging of the service life of the carbon anode is facilitated.

Description

System fluorine carbon anode mechanism
Technical field
The utility model belongs to system fluorine field, relates to a kind of system fluorine carbon anode mechanism.
Background technology
Electrolysis system fluorine is to lose electric charge through fluorion in the electrolytic solution at anode surface to be oxidized to fluorine gas; The desorption process that fluorion fluorine gas on anodic diffusion and the anode surface steeps in the solution all will lean on big as far as possible anode specific surface area; But because the space is limit in processing requirement and the groove, in electrolysis system fluorine technology, a kind of contradictory phenomena just occurred, increased electric current and help the increase of fluorine gas output; Make carbon anode produce polarization easily but electric current increases, can cause fluorine gas output to reduce again.
Summary of the invention
The utility model problem to be solved provides a kind of system fluorine carbon anode mechanism, and solving has big as far as possible carbon anode surface-area in the restriction fluorine groove, improves output, reduces cost, and reduces polar and takes place.
For realizing above-mentioned purpose, the technical scheme that the utility model is taked is:
A kind of system fluorine carbon anode mechanism comprises the carbon anode plate, and said carbon anode plate surface is provided with axial recess.
Said groove is a dovetail groove.
Said trapezoidal groove depth 8mm, last hem width 10mm, following bottom width 6mm.
The utility model carbon anode plate is provided with groove, and solving has big as far as possible carbon anode surface-area in the restriction fluorine groove, helps under original equipment situation, improving output, reduces cost, and reduces polar and takes place, and helps prolonging the carbon anode life-span.
Description of drawings
Fig. 1 the utility model structural representation.
Fig. 2 the utility model structure vertical view.
Fig. 3 the utility model structure A-A sectional view.
Embodiment
As shown in Figure 1, be the synoptic diagram of the utility model structure, a kind of system fluorine carbon anode mechanism comprises carbon anode plate 1, and carbon anode plate 1 surface is provided with axial recess 2, and groove is a dovetail groove, and carbon anode plate 1 inside is axially arranged with two upper screwed holes 3, is used to connect lead; Fig. 2 is the utility model structure vertical view, and trapezoidal groove depth H is 8mm, and top L is 10mm, and the W that goes to the bottom is 6mm; Fig. 3 the utility model structure A-A sectional view, threaded hole 3 is positioned at carbon anode plate 1 inside.
The carbon anode plate variable size that this use is novel is an example with 600 * 180 * 50mm carbon electrode plate, calculates by immersing ionogen 500mm; Surface-area is 0.23 ㎡, adopts the utility model surface-area can increase to 0.386 ㎡, and carbon anode and ionogen contact area have added 67.8%; Increase effectively carbon anode and ionogen contact area, improved fluorine gas output, under the situation of big electric current input, still keep the low current density in carbon anode surface; Reduced the generation of polarization phenomena; Stopped the depolarize operation, thereby prolonged the carbon anode life-span, obtained reducing production costs and improved the purpose of production capacity.
Through example, the concrete application of the utility model is described below:
Example 1, certain 4KA of company electrolyzer, former bath voltage 9.5V, electric current 4000A start and after 3 days polarization phenomena just take place, and in process of depolarization, cause a large amount of carbon anodes phenomenon that fractures; After using the utility model instead, promptly use the dull and stereotyped carbon plate of 600 * 180 * 5mm, on the carbon anode plate, be provided with groove; Groove is a dovetail groove, trapezoidal groove depth 8mm, last hem width 10mm; Following bottom width 6mm, bath voltage is reduced to 9.1V, and current boost is to 4500A; But carbon anode is lower than originally with the electrolyte interface watt current, and 0.05A/cm2 has used 4 months and polarization phenomena still do not occurred; The fluorine gas rate ratio is not used the every groove of this product fecund every day fluorine gas 7.6kg, and carbon anode plate life cycle is for 300 days, and ton fluorine gas production cost has descended 800 yuan.
Example 2, the red Ward kind of the preceding center gas 3000A of Leshan branch office of limited-liability company electrolyzer, when the dull and stereotyped carbon plate that uses 600 * 180 * 50, mean current 2900A; Average cell voltage 9.7V, mean lifetime 73 days uses the utility model on 2 electrolyzers, to test; Still operational excellence after 125 days; Mean current 2950A, average cell voltage 9.2V on average economizes on electricity more than 5%.
The carbon slab that example 3, the red Ward kind of the preceding center gas 10KA of Wenjiang company of limited-liability company electrolyzer use is 600 * 300 * 70mm, opposes than test with 4, and wherein 2 with in the past dull and stereotyped carbon slab; Use the utility model for other 2, at the test initial stage, polarization phenomena all appear in dull and stereotyped carbon slab; And polarization phenomena all do not appear in the carbon slab of fluting, and test current all is controlled at 9000A, after 2 months; Wherein polarization phenomena appear in 1 dull and stereotyped carbon slab once more, and depolarize is handled the back and recovered normal, the contrast potential situation; 2 dull and stereotyped carbon slab electrolyzer average voltages are 9.5V, and 2 fluting carbon slab average voltages are 9.1V, find out that the fluting carbon slab can economize on electricity more than 4.2%.

Claims (3)

1. a system fluorine carbon anode mechanism comprises the carbon anode plate, and it is characterized in that: said carbon anode plate surface is provided with axial recess.
2. system fluorine carbon anode according to claim 1 mechanism, it is characterized in that: said groove is a dovetail groove.
3. system fluorine carbon anode according to claim 2 mechanism is characterized in that: said trapezoidal groove depth 8mm, last hem width 10mm, following bottom width 6mm.
CN201220070442XU 2012-02-29 2012-02-29 Fluorite-preparing carbon anode mechanism Expired - Fee Related CN202492587U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220070442XU CN202492587U (en) 2012-02-29 2012-02-29 Fluorite-preparing carbon anode mechanism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220070442XU CN202492587U (en) 2012-02-29 2012-02-29 Fluorite-preparing carbon anode mechanism

Publications (1)

Publication Number Publication Date
CN202492587U true CN202492587U (en) 2012-10-17

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220070442XU Expired - Fee Related CN202492587U (en) 2012-02-29 2012-02-29 Fluorite-preparing carbon anode mechanism

Country Status (1)

Country Link
CN (1) CN202492587U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104671363A (en) * 2015-04-08 2015-06-03 南京大学连云港高新技术研究院 Gd-doped titanium-based Sb-SnO2 catalytic polar plate and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104671363A (en) * 2015-04-08 2015-06-03 南京大学连云港高新技术研究院 Gd-doped titanium-based Sb-SnO2 catalytic polar plate and preparation method thereof

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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

Granted publication date: 20121017

Termination date: 20170229

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