CN207259568U - A kind of distillation reaction dross cylinder - Google Patents

A kind of distillation reaction dross cylinder Download PDF

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Publication number
CN207259568U
CN207259568U CN201721044062.8U CN201721044062U CN207259568U CN 207259568 U CN207259568 U CN 207259568U CN 201721044062 U CN201721044062 U CN 201721044062U CN 207259568 U CN207259568 U CN 207259568U
Authority
CN
China
Prior art keywords
cylinder
drainage plate
dross
wall
current divider
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
CN201721044062.8U
Other languages
Chinese (zh)
Inventor
赵军朋
徐成哲
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.)
Anshan Massive Titanium Industry Co Ltd
Original Assignee
Anshan Massive Titanium Industry 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 Anshan Massive Titanium Industry Co Ltd filed Critical Anshan Massive Titanium Industry Co Ltd
Priority to CN201721044062.8U priority Critical patent/CN207259568U/en
Application granted granted Critical
Publication of CN207259568U publication Critical patent/CN207259568U/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model discloses a kind of distillation reaction dross cylinder, including cylinder, and the current divider being arranged in cylinder, and the reaction zone below cylinder, it is characterised in that:Diffluence pass is equipped with the top of the current divider, the diffluence pass is in inverted pyrometric cone, the bottom of the diffluence pass is connected by evaporation channel with the reaction zone, the drainage plate of annular is equipped with the inner wall of the cylinder, the groove of annular is equipped with the outer wall of the current divider, the front end of the drainage plate is located at the top of the groove, because drainage plate is equipped with the inner wall of dross cylinder, and it is equipped with groove in the lower section of drainage plate, when so when part, gaseous magnesium becomes liquid to the cold, the magnesium of liquid is just flowed into groove along the inner wall and drainage plate of dross cylinder, liquid magnesium is avoided to flow into gap, so as to reduce the difficulty of later stage cleaning work, greatly improve the efficiency of cleaning work.

Description

A kind of distillation reaction dross cylinder
Technical field
It the utility model is related to a kind of dross cylinder, especially a kind of distillation reaction dross cylinder.
Background technology
In the production process of titanium sponge, there are gap between current divider and dross cylinder, due to dross cylinder be provided in it is cold In condenser, so in volatilization process, gaseous volatile matter can become liquid to volatile matter to the cold, then along the inner wall of dross cylinder Flow at the gap between dross cylinder and current divider, be all magnesium chloride since volatile matter is most of, so after magnesium chloride cools down It will be sticked at gap, in the processing procedure in later stage, when the magnesium chloride in gap is cleared up, not only clear up time-consuming expense Power, but also be difficult to clean up clean.
Utility model content
The technical assignment of the utility model is to be directed to above the deficiencies in the prior art, and provides a kind of distillation reaction dross Cylinder.
Technical solution is used by the utility model solves its technical problem:A kind of distillation reaction dross cylinder, including Cylinder, and the current divider being arranged in cylinder, and the reaction zone below cylinder, wherein being set at the top of the current divider There is diffluence pass, the diffluence pass is in inverted pyrometric cone, and the bottom of the diffluence pass is connected by evaporation channel and the reaction zone It is logical, the drainage plate of annular is equipped with the inner wall of the cylinder, the groove of annular is equipped with the outer wall of the current divider, it is described The front end of drainage plate is located at the top of the groove.
Further improve:The current divider includes supporting table and shunting platform, and the shunting platform is located above supporting table, described The diameter for shunting platform bottom surface is less than the diameter of support countertop, and the groove is located at the top surface of supporting table.
Further improve:The supporting table is cylinder, and the shunting platform is round platform.
Further improve:The section of the drainage plate is triangular in shape.
Further improve:The rectangular triangle in section of the drainage plate, face and cylinder where a right-angle side it is interior Wall connects, face-up where bevel edge.
The advantages of the utility model:Because being equipped with drainage plate on the inner wall of dross cylinder, and set below drainage plate Fluted, so when a part of gaseous magnesium chloride becomes liquid to the cold, the magnesium of liquid just along the inner wall of dross cylinder and draws Flowing plate is flowed into groove, is avoided liquid magnesium and is flowed into gap, so as to reduce the difficulty of later stage cleaning work, greatly improves The efficiency of cleaning work.
Brief description of the drawings
Fig. 1 is the utility model structure diagram.
Embodiment
The utility model is described below with reference to Figure of description.
As shown in the figure, a kind of distillation reaction dross cylinder, including cylinder 2, and the current divider 4 being arranged in cylinder 2, and Reaction zone 5 positioned at the lower section of cylinder 2, wherein being equipped with diffluence pass 7 at the top of the current divider 4, the diffluence pass 7 is in inverted Pyrometric cone, the bottom of the diffluence pass 7 are connected with the reaction zone 5 by evaporation channel 6, are set on the inner wall of the cylinder 2 There is the drainage plate 3 of annular, the groove 8 of annular is equipped with the outer wall of the current divider 4, the front end of the drainage plate 3 is located at institute State the top of groove 8;The current divider 4 includes supporting table 41 and shunting platform 42, and the shunting platform 42 is located in supporting table 41 Side, the diameter of 42 bottom surface of the shunting platform are less than the diameter of 41 top surface of supporting table, and the groove 8 is located at the top surface of supporting table 41; The supporting table 41 is cylinder, and the shunting platform 42 is round platform;The section of the drainage plate 3 is triangular in shape;When drainage plate 3 The rectangular triangle in section when, the face where a right-angle side is connected with the inner wall of cylinder 2, face-up where bevel edge.
Its operation principle is:Being initially positioned at the evaporant in reaction zone 5 can reach at diffluence pass 7 along evaporation channel 6, because It is in inverted triangular pyramidal for diffluence pass 7, so evaporant can uniformly disperse away, since cylinder 2 is provided in condensation In device 1, so when evaporant runs into the inner wall of cylinder 2, become liquid from gaseous state, then the inner wall along cylinder 2, which flows to, draws In flowing plate 3, then again through drainage plate 3 flow into groove 8 in, so as to avoid liquid magnesium chloride flow into gap 9 in situation, into And mitigate the difficulty of post-processing work, improve the effect of cleaning.
The above description is only the embodiments of the present invention, and it does not limit the scope of the patent of the present invention, every Equivalent structure or equivalent flow shift made based on the specification and figures of the utility model, is directly or indirectly used in Other related technical areas, are equally included in the patent within the scope of the utility model.

Claims (5)

1. a kind of distillation reaction dross cylinder, including cylinder, and the current divider being arranged in cylinder, and below cylinder Reaction zone, it is characterised in that:Diffluence pass is equipped with the top of the current divider, the diffluence pass is in inverted pyrometric cone, described The bottom of diffluence pass is connected by evaporation channel with the reaction zone, and the drainage plate of annular is equipped with the inner wall of the cylinder, The groove of annular is equipped with the outer wall of the current divider, the front end of the drainage plate is located at the top of the groove.
A kind of 2. distillation reaction dross cylinder according to claim 1, it is characterised in that:The current divider includes supporting table With shunting platform, the shunting platform is located above supporting table, and the diameter of the shunting platform bottom surface is less than the diameter of support countertop, institute State the top surface that groove is located at supporting table.
A kind of 3. distillation reaction dross cylinder according to claim 2, it is characterised in that:The supporting table is cylinder, The shunting platform is round platform.
A kind of 4. distillation reaction dross cylinder according to claims 1 to 3 wherein any one, it is characterised in that:It is described The section of drainage plate is triangular in shape.
A kind of 5. distillation reaction dross cylinder according to claim 4, it is characterised in that:The section of the drainage plate is in straight Angle triangle, the inner wall in face and cylinder where a right-angle side connects, face-up where bevel edge.
CN201721044062.8U 2017-08-21 2017-08-21 A kind of distillation reaction dross cylinder Expired - Fee Related CN207259568U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721044062.8U CN207259568U (en) 2017-08-21 2017-08-21 A kind of distillation reaction dross cylinder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721044062.8U CN207259568U (en) 2017-08-21 2017-08-21 A kind of distillation reaction dross cylinder

Publications (1)

Publication Number Publication Date
CN207259568U true CN207259568U (en) 2018-04-20

Family

ID=61925879

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721044062.8U Expired - Fee Related CN207259568U (en) 2017-08-21 2017-08-21 A kind of distillation reaction dross cylinder

Country Status (1)

Country Link
CN (1) CN207259568U (en)

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GR01 Patent grant
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: 20180420

Termination date: 20210821