CN212771012U - Anti-crystallization emptying pipeline device for crude foil machine - Google Patents

Anti-crystallization emptying pipeline device for crude foil machine Download PDF

Info

Publication number
CN212771012U
CN212771012U CN202021383887.4U CN202021383887U CN212771012U CN 212771012 U CN212771012 U CN 212771012U CN 202021383887 U CN202021383887 U CN 202021383887U CN 212771012 U CN212771012 U CN 212771012U
Authority
CN
China
Prior art keywords
tank
pipeline
filter
electrolyte
liquid discharge
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.)
Active
Application number
CN202021383887.4U
Other languages
Chinese (zh)
Inventor
郭小高
胡增开
江先宗
陈亮龙
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.)
Fujian Clear View Copper Foils Co ltd
Original Assignee
Fujian Clear View Copper Foils 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 Fujian Clear View Copper Foils Co ltd filed Critical Fujian Clear View Copper Foils Co ltd
Priority to CN202021383887.4U priority Critical patent/CN212771012U/en
Application granted granted Critical
Publication of CN212771012U publication Critical patent/CN212771012U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The utility model discloses a prevent crystallization evacuation piping installation for giving birth to paper tinsel machine, it includes from the height to low setting gradually: the high-level tank is used for containing electrolyte, the anode tank is used for generating foil through the reaction of the electrolyte, and the filter is used for communicating the high-level tank with the anode tank to filter the electrolyte flowing into the anode tank from the high-level tank; the low-order groove, first connecting tube for connect high-order groove and filter, the second connecting tube for connect filter and anode tank, drainage tube for with remaining electrolyte discharge in the device when stopping using, the flowing back tee bend for connect drainage tube and second connecting tube, backflow pipeline for retrieve the electrolyte that flows from the anode tank. Obviously reduce the use amount of pipelines and pipe fittings, reduce the cost and reduce the leakage and the loss of the electrolyte washed away when the crystallization is generated. Compared with the traditional zero discharge operation, the operation process is simplified, the probability of error operation is reduced, and the production efficiency is improved.

Description

Anti-crystallization emptying pipeline device for crude foil machine
Technical Field
The utility model discloses be applied to living paper tinsel technology field, specifically be a prevent crystallization evacuation piping installation for living paper tinsel machine.
Background
Give birth to paper tinsel machine system in order to prevent that pipeline crystallization from influencing the crude paper tinsel quality in later stage and can discharge the electrolyte that remains in system and pipe fitting after stopping using, prior art adopts the segmentation to connect zero pipeline discharge method of discharging when guaranteeing to stop using pipe-line transportation electrolyte in making things convenient for the pipeline to discharge, has increased the pipe fitting use amount and the operation degree of difficulty. The zero-discharge pipe generally uses a pipe (DN15-40) with a smaller diameter, wherein the small-diameter pipe is easy to block and is especially obvious after the temperature of the electrolyte drops. The liquid inlet pipeline and the slag discharge pipeline share one pipeline, so that the length is large, the slag is remained more, and the product quality is not improved. One section of the filter is shared by zero discharge and filter zero discharge, while the filter generally adopts a general corrosion-resistant filter, and the bottom zero discharge port is small (DN15) and is easy to crystallize. Electrolyte in the filter is not easy to discharge, and the operation is difficult when the filter element needs to be replaced. Different pipe diameters arrange zero pipeline and finally receive same root pipeline on, it is inside to make electrolyte enter into other row zero pipelines of lower position easily to arrange zero in the higher position, causes the secondary crystallization risk.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that to prior art not enough, provide a prevent crystallization evacuation piping installation for giving birth to paper tinsel machine.
In order to solve the technical problem, the utility model discloses a prevent crystallization evacuation piping installation for giving birth to paper tinsel machine, it includes from the height to low setting gradually:
the elevated tank is used for containing electrolyte, an outlet is arranged at one side of the elevated tank, and an outlet valve is arranged at the outlet;
the anode tank is used for generating foil by the reaction of the electrolyte, a liquid inlet of the anode tank is arranged in the middle of the lower end of the anode tank, and liquid outlets of the anode tank are arranged on two sides of the upper end of the anode tank;
the filter is used for communicating the elevated tank and the anode tank to filter the electrolyte flowing into the anode tank from the elevated tank;
the low tank is arranged at the lowest position and used for recovering the electrolyte;
the first connecting pipeline is used for connecting the elevated tank and the filter, one end of the first connecting pipeline is connected with an outlet valve at the outlet of the elevated tank, and the other end of the first connecting pipeline is connected with the inlet of the filter;
the second connecting pipeline is used for connecting the filter and the anode tank, one end of the second connecting pipeline is connected with the outlet of the filter, and the other end of the second connecting pipeline is connected with the liquid inlet of the anode tank;
the liquid discharge pipeline is used for discharging the electrolyte remained in the device when the device is stopped, one end of the liquid discharge pipeline is connected with the middle section of the second connecting pipeline through a liquid discharge tee joint, and the other end of the liquid discharge pipeline is connected with the low-level tank;
the liquid discharge tee joint is used for connecting the liquid discharge pipeline with the second connecting pipeline, a liquid discharge valve is arranged at the liquid discharge end of the liquid discharge tee joint, and a flow blocking piece is arranged in the water through transverse pipe of the liquid discharge tee joint;
and the return pipeline is used for recovering the electrolyte flowing out of the anode tank, one end of the return pipeline is connected with liquid outlets on two sides of the anode tank, and the other end of the return pipeline is connected with the low tank.
As a possible embodiment, further, the inlet of the filter is higher than the outlet of the filter.
As a preferred option, preferably, a pipeline valve is arranged in the middle section of the first connecting pipeline.
As a possible implementation mode, further, the flow blocking piece is fixed in the center of the upper wall of the inner side of the drainage tee water pipe, and the cross section of the flow blocking piece is in an inverted triangle shape.
The utility model adopts the above technical scheme, following beneficial effect has:
1. the utility model discloses obviously reduce the use amount of pipeline, pipe fitting, reduce cost reduces and runs out the electrolyte loss that leaks and wash when producing the crystallization. Compared with the traditional zero discharge operation, the operation process is simplified, the probability of error operation is reduced, and the production efficiency is improved.
2. The utility model discloses a set up the flowing back tee bend with the feed liquor with arrange sediment pipeline phase separation, the residue secondary pollution that reduces greatly improves product quality. Through set up in the flowing back tee bend and keep off a class spare for can strike the preceding section pipeline of flowing back valve at electrolyte flow in-process, increase the flowing back valve upper portion and divide liquid mobility, solved among the prior art electrolyte and often because of the temperature that mobility descends and the crystallization card drains off the valve, thereby lead to unable evacuation to plug up the problem of pipeline.
Drawings
The present invention will be described in further detail with reference to the following drawings and embodiments:
FIG. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic structural view of a drainage tee in embodiment 1 of the present invention;
fig. 3 is a schematic structural view of a drainage tee in embodiment 2 of the present invention;
fig. 4 is a schematic view of a drainage tee joint according to embodiment 3 of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the drawings of the embodiments of the present invention will be combined to clearly and completely describe the technical solutions of the embodiments of the present invention.
Example 1
As shown in fig. 1-2, the utility model provides a prevent crystallization evacuation piping installation for living paper tinsel machine, it includes from high to low setting gradually:
the elevated tank 1 is used for containing electrolyte, an outlet is formed in one side of the elevated tank, and an outlet valve 101 is arranged at the outlet;
an anode tank 2 for generating foil by the reaction of the electrolyte, wherein a liquid inlet is arranged in the middle of the lower end, and liquid outlets are arranged on two sides of the upper end; an anode tank valve is arranged at the liquid inlet of the anode tank 2;
the filter 3 is used for communicating the elevated tank 1 and the anode tank 2 to filter the electrolyte flowing into the anode tank 2 from the elevated tank 1;
a low tank 4 arranged at the lowest position for recovering the electrolyte;
the first connecting pipeline 5 is used for connecting the elevated tank 1 and the filter 3, one end of the first connecting pipeline is connected with the outlet valve 101 at the outlet of the elevated tank 1, and the other end of the first connecting pipeline is connected with the inlet of the filter 3;
the second connecting pipeline 6 is used for connecting the filter 3 with the anode tank 2, one end of the second connecting pipeline is connected with the outlet of the filter 3, and the other end of the second connecting pipeline is connected with the liquid inlet of the anode tank 2;
the liquid discharge pipeline 7 is used for discharging the electrolyte remained in the device when the device is stopped, one end of the liquid discharge pipeline is connected with the middle section of the second connecting pipeline 6 through a liquid discharge tee joint 8, and the other end of the liquid discharge pipeline is connected with the low-level tank 4;
the liquid discharge tee joint 8 is used for connecting the liquid discharge pipeline 7 with the second connecting pipeline 6, a liquid discharge valve 801 is arranged at the liquid discharge end of the liquid discharge tee joint, and a flow blocking piece 802 is arranged in a horizontal water pipe of the liquid discharge tee joint;
and the return pipeline 9 is used for recovering the electrolyte flowing out of the anode tank 2, one end of the return pipeline is connected with liquid outlets on two sides of the anode tank 2, and the other end of the return pipeline is connected with the low tank 4.
As a possible embodiment, further, the inlet of the filter 3 is higher than the outlet of the filter 3.
As a better option, it is preferable that a pipeline valve 501 is provided in the middle of the first connecting pipeline 5.
As a possible implementation manner, further, the flow blocking piece 802 is fixed in the center of the upper wall of the inner side of the water flowing transverse pipe of the liquid discharging tee 8, the cross section of the flow blocking piece 802 is in the shape of an inverted triangle, and the height of the inverted triangle is higher than half of the pipe diameter of the water flowing transverse pipe of the liquid discharging tee 8.
In the course of the work, when carrying out the foil production during operation, the operator closes flowing back valve 801 of flowing back tee bend 8, open outlet valve 101 and pipeline valve 501, make the electrolyte in head tank 1 flow into filter 3 through first connecting tube 5 and filter the back and flow into anode tank 2 reaction and carry out the foil production operation, when the device stop work, in order to prevent that the pipeline crystallization from influencing the electrolyte that later stage foil production quality need will remain in system and pipe fitting after the exhaust of using, the operator closes outlet valve 101 this moment, and open flowing back valve 801, make the electrolyte that remains in the device system flow through flowing back valve 801 down through flowing back pipeline 7 and discharge zero by retrieving through first connecting tube 5 and second connecting tube 6.
Example 2
As shown in fig. 3, the difference between this embodiment and embodiment 1 is that the flow blocking member 802 is an inclined baffle, and the angle between the inclined baffle and the upper wall of the inner side of the horizontal pipe through which the liquid discharge tee 8 leads to is 30 to 45 °, and the electrolyte impacts the inclined baffle in the flowing process and continuously impacts the pipeline at the front end of the liquid discharge valve through refraction, and then flows out, so that the fluidity of the liquid on the liquid discharge valve is increased, and the problem that the liquid discharge valve is blocked by crystallization due to the temperature drop caused by the fluidity drop of the electrolyte in the prior art, so that the pipeline cannot be blocked by emptying is solved.
Example 3
As shown in fig. 4, the difference between this embodiment and embodiment 1 is that the flow blocking member 802 is a baffle perpendicular to the inner upper wall of the horizontal water pipe, one end of the baffle is an arc surface, and one end of the arc surface extends into the three-way drain pipe 8 and is located above the liquid discharge valve 801, and the electrolyte flows out of the horizontal water pipe after flowing through the top of the three-way drain pipe 801 in the three-way drain pipe 8 due to the blocking of the flow blocking member 802, so as to increase the fluidity of the liquid in the upper portion of the liquid discharge valve, thereby solving the problem that the electrolyte is usually crystallized and locked due to the temperature drop caused by the fluidity drop in the prior art, and the pipeline cannot be emptied.
The above embodiments are the embodiments of the present invention, and for those skilled in the art, according to the teaching of the present invention, the equivalent changes, modifications, replacements and variations made by the claims of the present invention should all belong to the scope of the present invention without departing from the principle and spirit of the present invention.

Claims (4)

1. The utility model provides a prevent crystallization evacuation piping installation for giving birth to paper tinsel machine which characterized in that: it includes from high to low setting gradually:
the elevated tank is used for containing electrolyte, an outlet is arranged at one side of the elevated tank, and an outlet valve is arranged at the outlet;
the anode tank is used for generating foil by the reaction of the electrolyte, a liquid inlet of the anode tank is arranged in the middle of the lower end of the anode tank, and liquid outlets of the anode tank are arranged on two sides of the upper end of the anode tank;
the filter is used for communicating the elevated tank and the anode tank to filter the electrolyte flowing into the anode tank from the elevated tank;
the low tank is arranged at the lowest position and used for recovering the electrolyte;
the first connecting pipeline is used for connecting the elevated tank and the filter, one end of the first connecting pipeline is connected with an outlet valve at the outlet of the elevated tank, and the other end of the first connecting pipeline is connected with the inlet of the filter;
the second connecting pipeline is used for connecting the filter and the anode tank, one end of the second connecting pipeline is connected with the outlet of the filter, and the other end of the second connecting pipeline is connected with the liquid inlet of the anode tank;
the liquid discharge pipeline is used for discharging the electrolyte remained in the device when the device is stopped, one end of the liquid discharge pipeline is connected with the middle section of the second connecting pipeline through a liquid discharge tee joint, and the other end of the liquid discharge pipeline is connected with the low-level tank;
the liquid discharge tee joint is used for connecting the liquid discharge pipeline with the second connecting pipeline, a liquid discharge valve is arranged at the liquid discharge end of the liquid discharge tee joint, and a flow blocking piece is arranged in the water through transverse pipe of the liquid discharge tee joint;
and the return pipeline is used for recovering the electrolyte flowing out of the anode tank, one end of the return pipeline is connected with liquid outlets on two sides of the anode tank, and the other end of the return pipeline is connected with the low tank.
2. The anti-crystallization emptying pipe device for the green foil machine as claimed in claim 1, wherein: the inlet of the filter is higher than the outlet of the filter.
3. The anti-crystallization emptying pipe device for the green foil machine as claimed in claim 1, wherein: and a pipeline valve is arranged in the middle section of the first connecting pipeline.
4. The anti-crystallization emptying pipe device for the green foil machine as claimed in claim 1, wherein: the flow blocking piece is fixed in the center of the upper wall of the inner side of the liquid discharge tee water passing transverse pipe, and the cross section of the flow blocking piece is in an inverted triangle shape.
CN202021383887.4U 2020-07-14 2020-07-14 Anti-crystallization emptying pipeline device for crude foil machine Active CN212771012U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202021383887.4U CN212771012U (en) 2020-07-14 2020-07-14 Anti-crystallization emptying pipeline device for crude foil machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202021383887.4U CN212771012U (en) 2020-07-14 2020-07-14 Anti-crystallization emptying pipeline device for crude foil machine

Publications (1)

Publication Number Publication Date
CN212771012U true CN212771012U (en) 2021-03-23

Family

ID=75079111

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202021383887.4U Active CN212771012U (en) 2020-07-14 2020-07-14 Anti-crystallization emptying pipeline device for crude foil machine

Country Status (1)

Country Link
CN (1) CN212771012U (en)

Similar Documents

Publication Publication Date Title
CN212771012U (en) Anti-crystallization emptying pipeline device for crude foil machine
CN210764360U (en) Saturator liquid seal tank
CN204323908U (en) Raw material pail discharging device
CN2350522Y (en) Negative pressure blow-off device
CN206715400U (en) A kind of whole-automatic double-drum aeration type filter
CN206492497U (en) A kind of chlorination safety production system
CN109604267B (en) Bidirectional cleaning device for mold waterway
CN205062904U (en) Can automatic clear up overflow arrangement of cistern deposit
CN205973789U (en) Hydrogen peroxide solution production oxidation process gas -liquid separation
CN206940999U (en) A kind of anti-flow structure of collaborating of Winning cell
CN205843296U (en) A kind of aluminum bits wind send dehydrator
CN217745855U (en) Product sedimentation layering recovery device in centrifugal wastewater
CN210710867U (en) Water-resin automatic discharger
CN210216584U (en) Water tank for vacuum pump
CN215864855U (en) Channel block structure convenient to pipeline backward flow separation
CN214305832U (en) Anti-siphon drainage structure of bottle washing machine
CN211938132U (en) Quartz wafer cleaning machine effluent recovery unit
CN211813532U (en) Process water recovery tank
CN212133436U (en) Horizontal type flash tank
CN215823843U (en) Receive milk cleaning system
CN213556304U (en) Alkali wash tower for producing medical intermediate
CN214470237U (en) Heat exchanger for charging and discharging
CN221274077U (en) Inclined bottom fluosilicic acid storage tank
CN218421982U (en) Device for washing and recycling exhaust gas in polyolefin catalyst production
CN206206892U (en) A kind of device for eliminating heating steam exhaust piping water hammer

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant