CN2782715Y - High-efficient acid bathing filter - Google Patents
High-efficient acid bathing filter Download PDFInfo
- Publication number
- CN2782715Y CN2782715Y CN 200520081286 CN200520081286U CN2782715Y CN 2782715 Y CN2782715 Y CN 2782715Y CN 200520081286 CN200520081286 CN 200520081286 CN 200520081286 U CN200520081286 U CN 200520081286U CN 2782715 Y CN2782715 Y CN 2782715Y
- Authority
- CN
- China
- Prior art keywords
- pipe
- acid
- tube
- main casing
- filtering
- 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 - Lifetime
Links
- 239000002253 acid Substances 0.000 title claims abstract description 37
- 238000003287 bathing Methods 0.000 title abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000004744 fabric Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000001471 micro-filtration Methods 0.000 claims description 11
- 239000003513 alkali Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 abstract description 19
- 238000007789 sealing Methods 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000007664 blowing Methods 0.000 abstract description 2
- 238000007872 degassing Methods 0.000 abstract 2
- 230000006835 compression Effects 0.000 abstract 1
- 238000007906 compression Methods 0.000 abstract 1
- 239000012535 impurity Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000009987 spinning Methods 0.000 description 4
- 239000000084 colloidal system Substances 0.000 description 3
- 229920000297 Rayon Polymers 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 229920006253 high performance fiber Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
Images
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- Filtering Materials (AREA)
Abstract
The utility model relates to a high-efficient acid bathing filter. The utility model comprises a main shell body and an outer shell which is composed of an upper sealing head and a lower sealing head, wherein the upper sealing head is connected with an acid outlet pipe and a degassing pipe, the acid outlet pipe and the degassing pipe are connected with a blowing pipe of air compression and a cleaning water pipe, and the lower sealing head is connected with an acid inlet pipe; the lower part of the main shell body is provided with an acid fouling opening, the upper end of the inner part of the main shell body is provided with a pattern plate, a plurality of vertical micropore filtering pipes are arranged on the pattern plate, and the micropore filtering pipe is composed of a micropore pipe of which the pipe wall is provided with a plurality of micropores, filtering cloth which is coated on the surface of the micropore pipe and a diatomite layer which is uniformly attached to the surface the filtering cloth. The utility model has the advantages of large filtering quantity, high filtering precision, less inverse cleaning time and good effect and can not result in secondary pollution.
Description
Technical field
The utility model relates to the filter technology field, particularly relates to a kind of acid bath filter.
Background technology
In the chemical fibre spinning is produced, cellulose xanthate in spinning bath and the viscose glue and yellow byproduct reaction, generate a large amount of colloid sulphur, these colloid sulphur have with tiny Dispersion of Particles in acid bath, the colloid of forming that has floats on the bath face, in addition, also bring a large amount of impurity in viscose glue or in the acid bath allocation process into, make spinning bath become muddy, increase the spinning fault, reduce end product quality, and these impurity also can be deposited on the wall, bring obstacle to production process, therefore must be equipped with the acid bath filter acid bath is filtered.Existing acid bath filter mainly contains quartz sand filtration device and millipore filter.The former filtration yield is little, and filtering accuracy is low, and the backwash cycle is short, the time spent is many; There is the defective that filtration yield is little, filtering accuracy is low equally in the latter, is not suitable for producing high-performance fiber, and equipment is huge, and it is many to take factory building, has a large amount of acid water during backwash and discharges, and environment is polluted.
Summary of the invention
The purpose of this utility model is exactly at above-mentioned the deficiencies in the prior art, provides that a kind of filtration yield is big, filtering accuracy is high, the backwash cycle is long, few efficient acid bath filter of backwash time spent.
The efficient acid bath filter of the utility model, comprise by main casing and be connected upper cover on the main casing and shell that low head constitutes, the upper cover end face is provided with manhole, be connected with out acid tube and deaeration pipe on the upper cover, going out acid tube also is connected with the cleaning water pipe with the compressed air anti-blowpipe with deaeration pipe, be connected with acid inlet tube on the low head, the bottom of main casing is provided with dirty acid mouth.Interior upper end at main casing is installed with card, many vertical microfiltration tubes are installed on the card, microfiltration tube by tube wall have some micropores microporous pipe, be coated on the filter cloth on microporous pipe surface and evenly constitute attached to the diatomite layer on filter cloth surface.
Efficient as mentioned above acid bath filter, the micropore size on its microporous pipe is the 15-40 order.
Efficient as mentioned above acid bath filter, its diatomaceous particle diameter that forms diatomite layer is the 50-400 order.
Because the utility model forms a diatomite pre-filtering layer on the surface of microfiltration tube, and little, the adhesion in diatomite particle gap, increased the filter table area, strengthened the retaining power of filter medium, the rate of filtration and filtration yield under the condition that does not increase filtration resistance, have been improved, the filtering accuracy height.Because filtrate goes out on advancing under being when filtering, impurity segments cloth attached to slightly going up less, down on many under being on the microfiltration tube, blow under in the pipe by compressed air during backwash, impurity comes off rapidly under the effect of own wt and air-flow vibrations, the backwash time spent is few, effective, substantially do not wash with water, avoided secondary pollution.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
The specific embodiment
The accompanying drawing illustrated embodiment the utlity model has the shell of sealing, and shell is by columnar main casing 6, constitute by sending out the blue low head 19 that is connected the upper cover 3 of main casing 6 upper ends and is connected main casing 6 lower ends.Upper cover 3 end faces are provided with the manhole 2 that is used to check, are connected with out acid tube 1 and deaeration pipe 12 on the upper cover 3, go out acid tube 1 and also are connected with cleaning water pipe 11 with compressed air anti-blowpipe 10 with deaeration pipe 12.On low head 19, be connected with acid inlet tube 20 and alkali inlet tube 9, and be fixed with support.Be connected with the positive blowpipe 5 of compressed air on the top of main casing 6, the bottom is provided with dirty acid mouth 8, and Pressure gauge 13 and visor 14 are equipped with in main casing 6 sides.Also be fixed with hanger 7 in main casing 6 sides.Have in the inner chamber of main casing 6 upper end by sending out hard-wired card 4 blue, be installed with many vertical microfiltration tubes 15 on the card 4, microfiltration tube 15 comprises that tube wall has the microporous pipe 16 that some pore sizes are 15-40 order micropore, be coated with one deck filter cloth 17 on the surface of microporous pipe 16, filter cloth 17 surfaces evenly are attached with one deck diatomite layer 18, and the diatomaceous particle size that constitutes diatomite layer 18 is the 50-400 order.During filtration, acid bath is advanced from acid inlet tube 20, goes out from going out acid tube 1, and constantly injects the diatomite turbid liquid betwixt.During backwash, the direct compressed air that enters by compressed air anti-blowpipe 10 is removed filter cake to microfiltration tube 15 blowbacks.For prolonging 15 service lifes of microfiltration tube, blowback repeatedly back adds the low concentration soda baths from alkali inlet tube 9 microfiltration tube 15 is regenerated, during just blowing repeatedly by the positive blowpipe 5 of compressed air, to improve regeneration effect.
Claims (4)
1, a kind of efficient acid bath filter, comprise by main casing (6) and be connected upper cover (3) on the main casing (6) and shell that low head (19) constitutes, upper cover (3) end face is provided with manhole (2), be connected with out acid tube (1) and deaeration pipe (12) on the upper cover (3), go out acid tube (1) and deaeration pipe (12) also with compressed air anti-blowpipe (10)) with clean water pipe (11) and be connected, be connected with acid inlet tube (20) on the low head (19), main casing (6) bottom is provided with dirty acid mouthful (8), it is characterized in that: be installed with card (4) in the interior upper end of main casing (6), many vertical microfiltration tubes (15) are installed on the card (4), and microfiltration tube (15) is had the microporous pipe (16) of some micropores by tube wall, be coated on the filter cloth (17) on microporous pipe (16) surface and evenly constitute attached to the diatomite layer (18) on filter cloth (17) surface.
2, efficient acid bath filter according to claim 1 is characterized in that the micropore size on the microporous pipe (16) is the 15-40 order.
3, efficient acid bath filter according to claim 1, the diatomaceous granularity that it is characterized in that forming diatomite layer (18) is the 50-400 order.
4, efficient acid bath filter according to claim 1 is characterized in that the top of main casing (6) is connected with the positive blowpipe of compressed air (5), is connected with alkali inlet tube (9) on the low head (19).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520081286 CN2782715Y (en) | 2005-03-19 | 2005-03-19 | High-efficient acid bathing filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520081286 CN2782715Y (en) | 2005-03-19 | 2005-03-19 | High-efficient acid bathing filter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2782715Y true CN2782715Y (en) | 2006-05-24 |
Family
ID=36767707
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200520081286 Expired - Lifetime CN2782715Y (en) | 2005-03-19 | 2005-03-19 | High-efficient acid bathing filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2782715Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107313116A (en) * | 2016-04-26 | 2017-11-03 | 兰州蓝星纤维有限公司 | A kind of exhaust apparatus and its application method for wet spinning spinning head |
CN107812401A (en) * | 2017-11-20 | 2018-03-20 | 宜宾丝丽雅股份有限公司 | A kind of pretreating process for viscose rayon spent lye |
-
2005
- 2005-03-19 CN CN 200520081286 patent/CN2782715Y/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107313116A (en) * | 2016-04-26 | 2017-11-03 | 兰州蓝星纤维有限公司 | A kind of exhaust apparatus and its application method for wet spinning spinning head |
CN107313116B (en) * | 2016-04-26 | 2023-04-07 | 兰州蓝星纤维有限公司 | Exhaust device for wet spinning nozzle and using method thereof |
CN107812401A (en) * | 2017-11-20 | 2018-03-20 | 宜宾丝丽雅股份有限公司 | A kind of pretreating process for viscose rayon spent lye |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CX01 | Expiry of patent term |
Expiration termination date: 20150319 Granted publication date: 20060524 |