CN209039596U - A kind of gas-liquid separation box - Google Patents
A kind of gas-liquid separation box Download PDFInfo
- Publication number
- CN209039596U CN209039596U CN201821203974.XU CN201821203974U CN209039596U CN 209039596 U CN209039596 U CN 209039596U CN 201821203974 U CN201821203974 U CN 201821203974U CN 209039596 U CN209039596 U CN 209039596U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid separation
- plate
- separation box
- section
- 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
Links
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to a kind of gas-liquid separation box, it is characterised in that the main body of gas-liquid separation box is bent by plate, forms bar shaped gap in the one side of corresponding inlet, the inner wall of the corresponding plate of bar shaped gap location is provided with mesh plate.The utility model optimizes the structure of gas-liquid separation box, improves feed liquor efficiency, reduces processing cost and difficulty.Therefore a kind of improved electric tank based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers of gas-liquid separation box assembling of the utility model has the advantages of improving structural reliability, improving system run all right, improve production efficiency, reduce processing cost.
Description
Technical field
The utility model relates to a kind of gas-liquid separation boxes.
Background technique
The BM-2.7 ion-exchange membrane electrolyzer for originating in German 5 enlightening (Uhde) company, mainly has the third generation in operation at present
~the six generation (V3, V4, V5, V6) groove profile.
It is existing in problem in China there are about the device of more than 400 ten thousand tons of caustic soda of annual output:
1, electrolytic cell mandril is locked, and because area is too small, yin-yang interpolar can generate the contact conduction between adjacent 2 groups because of resistance
The voltage of 30mV~60mV also has even higher, increase product power consumption, and fever is caused to promote temperature.
2, because the electrode base material of collector (titanium, nickel screen) is welded on gusset, gusset spacing is big, and wire side is because in electrolytic cell
The pressure oscillation deformation such as easy to form recessed or raised.
3, the sealing surface of anode unit is titanium, and noble coatings are done on surface prevents crevice corrosion, and a phase ionic membrane uses
As destroyed coating when cleaning sealing surface when replacement after complete, it is necessary to unit groove is integrally put into electric furnace burning and is paid, it is at high cost and easy
Cause unit groove to deform, have it is more because corrosion-inhibiting coating is done badly the case where causing sealing surface seriously corroded, maintenance more
It is difficult to change flatness to be kept.
4, unreasonable for loop structure (see Fig. 7) and gas-liquid Seperating box structure (see Fig. 8) inside electrolyte.
Summary of the invention
Purpose of the utility model is to overcome the above-mentioned shortcomings and provide a kind of gas-liquid separation boxes to be based on 5 enlightening for assembling
The improved electric tank of BM2.7 ion-exchange membrane electrolyzer.
Purpose of the utility model is realized as follows:
A kind of gas-liquid separation box, the main body of the gas-liquid separation box are bent by plate, are formed in the one side of corresponding inlet
The inner wall in bar shaped gap, the corresponding plate of bar shaped gap location is provided with mesh plate.
The main body of gas-liquid separation box is bent and is welded by two boards, and two boards are respectively the first plate and the second plate,
First plate includes the first oblique section of first horizontal segment and first horizontal segment right end oblique bending to the right, and the second plate includes the
Two horizontal segments, the left end of the second horizontal segment are vertically bent with vertical section upwards, and the upper end of vertical section is bent with to the right shorter water
Square to sealing welding section, the upper end of first horizontal segment and vertical section welded, and the right end of the second horizontal segment is to upper left side
It is bent with the second oblique section, in the same plane, and there are vertical between the first oblique section and the second oblique section for the second oblique section and the first oblique section
To bar shaped gap, the medial surface of the first oblique section and the second oblique section is welded with longitudinal mesh plate, the left side connection of vertical section
Liquid insertion tube out.
The length of first oblique section is 3-5 times of the second oblique segment length.
Compared with prior art, the utility model has the beneficial effects that
The utility model optimizes the structure of gas-liquid separation box, improves feed liquor efficiency, reduces processing cost and difficulty.Therefore
A kind of improved electric tank based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers of gas-liquid separation box assembling of the utility model, which has, to be improved
The advantages of structural reliability improves system run all right, improves production efficiency, reduce processing cost.
Detailed description of the invention
Fig. 1 is a kind of improved electric tank total figure based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers.
Fig. 2 is a kind of unit electrolytic bath group schematic diagram of improved electric tank based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers.
Fig. 3 is the improvement schematic diagram of conductive bar and gusset.
Fig. 4 is the film pole span structural schematic diagram of cathode electrode unit slot.
Fig. 5 is former circulation plates scheme of installation.
Fig. 6 is the utility model circulation plates scheme of installation.
Fig. 7 is Primordial Qi liquid Seperating box side view.
Fig. 8 is Primordial Qi liquid Seperating box front view.
Fig. 9 is the utility model gas-liquid separation box side view.
Figure 10 is the utility model gas-liquid separation box front view.
Wherein:
Truss 1
Unit electrolytic bath group 2, groove body frame 201, gas-liquid separation box 202, total plate 202.1, the first plate 202.2, the first water
Flat section 202.21, the first oblique section 202.22, the second plate 202.3, the second horizontal segment 202.31, vertical section 202.32, sealing welding
Section the 202.33, second oblique section 202.34, bar shaped gap 202.4, mesh plate 202.5, feed liquor dispersion pipe 203, feed liquor adapter tube 204,
Former gusset 205 goes out liquid insertion tube 206, goes out liquid adapter tube 207, anode unit electrolytic cell 208, cathode electrode unit electrolytic cell 209, cathode
The former conductive bar 210 of spacer screen 209.1, cathode elastic network(s) 209.2, cathode veil 209.3, new gusset 211, new conductive bar 212, circulation
Plate 213
Packing plate 3
Locked groove mandril 4
Rectifier 5.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
It clearly and completely describes, it is clear that described embodiment is only invention a part of the embodiment, instead of all the embodiments.
Based on the embodiments of the present invention, obtained by those of ordinary skill in the art without making creative efforts
Every other embodiment, fall within the protection scope of the utility model.
Referring to Fig. 1-Figure 10, the utility model relates to a kind of improved electric based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers
Slot is solved, it includes truss 1, and the multiple unit electrolytic bath groups 2 being vertically arranged, the list in left side are provided on the crossbeam of the truss 1
The left side of first electrolytic cell group 2 abuts vertical packing plate 3, and the right side of the unit electrolytic bath group 2 on right side is compeled against vertical
Tight plate 3, is connected with cross-brace between the packing plate 3 on right side and the right support of truss 1, the packing plate 3 in left side by one to
Right locked groove mandril 4 is held out against, so that two neighboring unit electrolytic bath group 2 is fitted closely and is electrically connected, two units at both ends
It is also electrically connected between electrolytic cell group 2 by rectifier 5.
Wherein:
Unit electrolytic bath group passes through flange moulding, screw by 1 anode unit electrolytic cell and 1 cathode electrode unit electrolytic cell
The composition such as group, insulation spacer, sealing strip, ionic membrane, anode is titanium (having titanium palladium alloy electrodes), and cathode is that nickel material (has electricity
Pole), specific:
Anode unit electrolytic cell and cathode electrode unit electrolytic cell include the groove body frame 201 of surrounding, shape in groove body frame 201
At anode chamber and cathode chamber, gas-liquid separation box 202, the bottom of anode chamber and cathode chamber are provided at the top of anode chamber and cathode chamber
Portion is provided with feed liquor dispersion pipe 203, and the inlet of feed liquor dispersion pipe 203 connects feed liquor adapter tube 204, anode chamber and cathode chamber
Middle part is provided with the former gusset 205 of more be vertically connected with, and circulation plates 213 are provided in anode chamber, and gas-liquid separation box 202 goes out liquid
Mouth is connected with downwards one and goes out liquid insertion tube 206, and the lower end of liquid insertion tube 206 connects out liquid adapter tube 207 out;Anode unit electrolysis
Slot and cathode electrode unit electrolytic cell be electrically connected to each other, and is provided with former conductive bar on one side in the electrical connection of anode unit electrolytic cell 208
210, the position of former conductive bar 210 corresponds to the position of the indoor former gusset 205 of internal anode, therefore in general adjacent two
Spacing between former conductive bar 210 is 130mm;
Now improved for the prior art:
1, keep former conductive bar 210,205 position of former gusset constant, to match with BM-2.7 type electricity slot, in former muscle
Several new gussets 211 are further added by between plate 205, the one side of the electrical connection of the anode unit electrolytic cell 208 of corresponding new gusset 211 increases
Add new conductive bar 212, so that contact conductive area increases, contact voltage is down to by reduction resistance for the increase of new conductive bar 212
10mV is hereinafter, in addition increased new gusset 211 enhances the intensity of entire unit groove.
Gap is formed between each adjacent two original gusset 205, new gusset 211 can be added in a gap, it can also be with every
New gusset 211 is added every two gaps, according to requiring to be selected.
2, the sealing surface of anode unit electrolytic cell 208 is changed to titanium palldium alloy, prevents crevice corrosion, be convenient to clean sealing
Face.
3, cathode electrode unit electrolytic cell 209 is changed to film pole span structure, which includes cathode electrode unit electrolytic cell 209
On the cathode spacer screen 209.1, cathode elastic network(s) 209.2 and the cathode veil 209.3 that are successively arranged outward.
4, it is provided with diagonally disposed circulation plates 213 in anode chamber, is different from the vertically arranged circulation of conventional
Plate.
5, optimize the structure of gas-liquid separation box 202:
The main body of original gas-liquid separation box is bent by one block of total plate 202.1, in the one side of inlet, total plate
202.1 two free ends are engaged, and processing technology is complex, and processing cost is high, in addition on total plate 202.1 uniformly into
Row aperture, forms inlet, and drill process is relatively complicated;
The main body of follow-on gas-liquid separation box of the utility model is bent and is welded by two boards, two plates
Matter is titanium or nickel, and two boards are respectively the first plate 202.2 and the second plate 202.3, and the first plate 202.2 includes first horizontal segment
202.21 and the oblique bending to the right of 202.21 right end of first horizontal segment the first oblique section 202.22, the second plate 202.3 packet
The second horizontal segment 202.31 is included, the left end of the second horizontal segment 202.31 is vertically bent with vertical section 202.32, vertical section upwards
202.32 upper end is bent with to the right the sealing welding section 202.33 of shorter horizontal direction, first horizontal segment 202.21 and perpendicular
The upper end of straight section 202.32 is welded, and the right end of the second horizontal segment 202.31 is bent with the second oblique section 202.34 to upper left side,
Second oblique section 202.34 and the first oblique section 202.22 in the same plane, and the first oblique section 202.22 and the second oblique section 202.34 it
Between there are longitudinal bar shaped gap 202.4, the length of the first oblique section 202.22 is 3-5 times of the second oblique 202.34 length of section, the
The medial surface of one oblique section 202.22 and the second oblique section 202.34 is welded with longitudinal mesh plate 202.5, vertical section 202.32
Left side connects out liquid insertion tube 206.It is low that difficulty is bent when this kind of gas-liquid separation box 202 not only makes, easy to process, feed liquor
Mouth is made of bar shaped gap 202.4 and mesh plate 202.5, without drilling operation is carried out while liquid inlet volume is larger, is saved
About cost and manufacturing procedure.
The above is only the specific application examples of the utility model, do not constitute any limit to the protection scope of the utility model
System.Any technical scheme formed by adopting equivalent transformation or equivalent replacement, all fall within the utility model rights protection scope it
It is interior.
Claims (3)
1. a kind of gas-liquid separation box, it is characterised in that the main body of gas-liquid separation box is bent by plate, the one of corresponding inlet
Face forms bar shaped gap, and the inner wall of the corresponding plate of bar shaped gap location is provided with mesh plate;
The main body of gas-liquid separation box is bent and is welded by two boards, and two boards are respectively the first plate (202.2) and second
Plate (202.3), the first plate (202.2) include first horizontal segment (202.21) and first horizontal segment (202.21) right end to bottom right
First oblique section (202.22) of the oblique bending in side, the second plate (202.3) include the second horizontal segment (202.31), the second horizontal segment
(202.31) left end is vertically bent with vertical section (202.32) upwards, and the upper end of vertical section (202.32) is bent with to the right shorter
Horizontal direction sealing welding section (202.33), first horizontal segment (202.21) and the upper end of vertical section (202.32) are welded
Connect, the right end of the second horizontal segment (202.31) is bent with the second oblique section (202.34) to upper left side, the second oblique section (202.34) with
In the same plane, and there are longitudinal directions between the first oblique section (202.22) and the second oblique section (202.34) for first oblique section (202.22)
Bar shaped gap (202.4), the medial surface of the first oblique section (202.22) and the second oblique section (202.34) is welded with longitudinal mesh
Plate (202.5), the left side of vertical section (202.32) connect out liquid insertion tube (206).
2. a kind of gas-liquid separation box according to claim 1, it is characterised in that: the length of the first oblique section (202.22) is the
3-5 times of two oblique section (202.34) length.
3. a kind of gas-liquid separation box according to claim 1, it is characterised in that: two boards material is titanium or nickel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821203974.XU CN209039596U (en) | 2018-07-27 | 2018-07-27 | A kind of gas-liquid separation box |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821203974.XU CN209039596U (en) | 2018-07-27 | 2018-07-27 | A kind of gas-liquid separation box |
Publications (1)
Publication Number | Publication Date |
---|---|
CN209039596U true CN209039596U (en) | 2019-06-28 |
Family
ID=67030008
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201821203974.XU Active CN209039596U (en) | 2018-07-27 | 2018-07-27 | A kind of gas-liquid separation box |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN209039596U (en) |
-
2018
- 2018-07-27 CN CN201821203974.XU patent/CN209039596U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
PL113658B1 (en) | Unipolar diaphragm cell | |
CN208517539U (en) | A kind of electrolytic cell being conveniently replaceable amberplex | |
WO2011082657A1 (en) | Bottom structure of electrolytic cell | |
CN209039596U (en) | A kind of gas-liquid separation box | |
CN208379020U (en) | A kind of compound electrode component | |
CN208980807U (en) | A kind of improved electric tank based on 5 enlightening BM2.7 ion-exchange membrane electrolyzers | |
CN109267087A (en) | A kind of a bipolar type ion-exchange membrane electrolyzer | |
CN203013539U (en) | Aluminum electrolytic capacitor used low-voltage anode foil corrosion electrolyzing device | |
US4075077A (en) | Electrolytic cell | |
CN208949423U (en) | A kind of novel a bipolar type ion-exchange membrane electrolyzer | |
CN101307466B (en) | Horizontal current aluminium cell | |
CN201158718Y (en) | Horizontal electrolytic aluminium electrolytic tank | |
CN208362488U (en) | A kind of electrolysis method prepares the universal cathode plate of high pure metal material | |
CN206843604U (en) | A kind of rare earth electrolysis cell enters electric structure | |
JP2008115455A (en) | Single/double pole type electrolyzer | |
CN110029359B (en) | Multi-chamber aluminum electrolytic cell and its busbar system | |
CN208183087U (en) | A kind of titanium painting ruthenium net anode plate of insoluble anode method electrolytic preparation high pure metal | |
CN201354386Y (en) | Aluminum electrolysis bath energy-saving cathode block structure | |
CN215713424U (en) | Integrally assembled bipolar diaphragm-free electrolysis device | |
CN206814857U (en) | A kind of chlorate electrolysis slot device | |
CN210736910U (en) | Ion membrane electrolytic tank | |
CN221501268U (en) | Cathode arm for reducing power consumption of electrolytic tank | |
CN203270054U (en) | Horizontal power inlet aluminium cell | |
CN220376801U (en) | An I-shaped cavity frame cathode device used in high-temperature melting electrolyzers | |
CN201809460U (en) | Electrolytic cell cathode sheet connecting structure |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: No.45, Xi'an Wei, Ligang Xi'an village, Lingang New Town, Jiangyin City, Wuxi City, Jiangsu Province Patentee after: Hongze (Jiangsu) Technology Co.,Ltd. Address before: No.45, Xi'an Wei, Ligang Xi'an village, Lingang New Town, Jiangyin City, Wuxi City, Jiangsu Province Patentee before: JIANGYIN HONGZE CHLORINE ALKALI EQUIPMENT MANUFACTURING Co.,Ltd. |
|
CP01 | Change in the name or title of a patent holder |