CN108553974A - Filter - Google Patents
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- Publication number
- CN108553974A CN108553974A CN201810604131.9A CN201810604131A CN108553974A CN 108553974 A CN108553974 A CN 108553974A CN 201810604131 A CN201810604131 A CN 201810604131A CN 108553974 A CN108553974 A CN 108553974A
- Authority
- CN
- China
- Prior art keywords
- filtrate
- transporting device
- helix transporting
- shell
- filtration system
- 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.)
- Pending
Links
- 239000000706 filtrate Substances 0.000 claims abstract description 26
- 238000001914 filtration Methods 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000007789 sealing Methods 0.000 claims abstract description 8
- 238000003828 vacuum filtration Methods 0.000 claims abstract description 8
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 4
- 238000004140 cleaning Methods 0.000 claims abstract description 4
- 239000003480 eluent Substances 0.000 claims abstract description 4
- 239000004744 fabric Substances 0.000 claims abstract description 4
- 239000002904 solvent Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000000047 product Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000012824 chemical production Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/05—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements supported
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/90—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/92—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging filtrate
Abstract
The invention discloses a kind of filters, it has conveying system, filtration system and vacuum filtration system successively, the conveying system is helix transporting device, helix transporting device has an axis being connected with the speed reducer of translator, the helical blade of fixed pitch gradual change on axis, one end of the shell of helix transporting device has feed inlet and filtrate (liquid, the other end of the shell of helix transporting device to have discharge port, the top of the shell of helix transporting device to have eluent solvent mouth；The cover top portion of the filtration system and the filtrate (liquid of helix transporting device are connected by sealing ring, there is filter cloth and sieve plate below sealing ring；The vacuum filtration system has filtrate tank and vacuum pump, has vacuum pipe interface, cleaning water inlet and filtrate feed inlet, filtrate feed inlet to be connected with the bottom of filtration system shell at the top of filtrate tank, vacuum pipe interface is connected by pipeline with vacuum pump.The advantage of the invention is that simple in structure, reliability is high, and filtering is at low cost, improves the quality and quantity of product.
Description
Technical field
The present invention relates to a kind of chemical production equipment, especially a kind of filter.
Background technology
Filter is to realize the important equipment being separated by solid-liquid separation, and is widely used in the productions such as chemical industry, medicine, conventional filter
Filter efficiency is low, and the consuming time is long, and filtering is of high cost, and the evaporating, emitting, dripping or leaking of liquid or gas phenomenon of material is also very serious, is brought to production environment
Prodigious destruction, directly influences the quality and the market competitiveness of product.
Invention content
For overcome the deficiencies in the prior art, the present invention provides it is a kind of it is simple in structure, production efficiency is high, safe and reliable
Filter.
The present invention adopts the following technical scheme that.
A kind of filter, it is spiral transferring to have conveying system, filtration system and vacuum filtration system, the conveying system successively
Sending device, helix transporting device has an axis being connected with the speed reducer of translator, the helical blade of fixed pitch gradual change on axis,
One end of the shell of helix transporting device has feed inlet and filtrate (liquid, the other end of the shell of helix transporting device to have discharging
Mouthful, eluent solvent mouth is arranged at the top of the shell of helix transporting device；The cover top portion and helix transporting device of the filtration system
Filtrate (liquid connected by sealing ring, have filter cloth and sieve plate below sealing ring；The vacuum filtration system has filtrate tank and true
Vacuum pipe interface, cleaning water inlet and filtrate feed inlet, filtrate feed inlet and filtration system shell are arranged at sky pump, filtrate tank top
Bottom be connected, vacuum pipe interface is connected by pipeline with vacuum pump.
Compared with the prior art, the advantages of the present invention are as follows simple in structure, reliability is high, and filtering is at low cost, substantially increases production
The quality and quantity of product, alleviate the labor intensity of operating personnel.
Description of the drawings
Fig. 1 is the structural schematic diagram of the embodiment of the present invention.
Specific implementation mode
Below in conjunction with drawings and examples, present invention is further described in detail.
As shown in Fig. 1, a kind of filter has conveying system, filtration system and vacuum filtration system, the conveying successively
System is helix transporting device 1, and helix transporting device 1 has an axis 103 being connected with the speed reducer 3 of translator 2, on axis 103
There are feed inlet 101 and filtrate (liquid 102 in one end of the helical blade 104 of fixed pitch gradual change, the shell of helix transporting device 1,
The other end of the shell of helix transporting device 1 has discharge port 106, the top of the shell of helix transporting device 1 to have eluent solvent mouth
105；4 top of shell of the filtration system is connect with the filtrate (liquid 102 of helix transporting device by sealing ring 7, sealing ring 7
There are filter cloth 6 and sieve plate 5 below.The vacuum filtration system has filtrate tank 8 and vacuum pump 9,8 top of filtrate tank to have vacuum pipe to connect
Mouth 802, cleaning water inlet 803 and filtrate feed inlet 801, filtrate feed inlet 801 are connected with the bottom of the shell 4 of filtration system,
Vacuum pipe interface 802 is connected by pipeline 11 with vacuum pump 9, and upper valve 12 is housed on pipeline 11, and 8 outside of filtrate tank is also equipped with
Liquid level gauge 804, filtrate pot bottom have liquid outlet 805, liquid outlet 805 to be connected with lower valve 13, and filtrate tank 8 is fixed by holder 10
On ground.
Claims (1)
1. a kind of filter, it is characterised in that have conveying system, filtration system and vacuum filtration system, the conveying system successively
For helix transporting device, helix transporting device has an axis being connected with the speed reducer of translator, fixed pitch gradual change on axis
There are a feed inlet and filtrate (liquid in helical blade, one end of the shell of helix transporting device, the shell of helix transporting device it is another
End has discharge port, the top of the shell of helix transporting device to have eluent solvent mouth；The cover top portion and spiral of the filtration system
The filtrate (liquid of conveying device is connected by sealing ring, there is filter cloth and sieve plate below sealing ring；The vacuum filtration system has filter
Vacuum pipe interface, cleaning water inlet and filtrate feed inlet, filtrate feed inlet and filtering are arranged at flow container and vacuum pump, filtrate tank top
The bottom of system shell is connected, and vacuum pipe interface is connected by pipeline with vacuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810604131.9A CN108553974A (en) | 2018-06-13 | 2018-06-13 | Filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810604131.9A CN108553974A (en) | 2018-06-13 | 2018-06-13 | Filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108553974A true CN108553974A (en) | 2018-09-21 |
Family
ID=63553520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810604131.9A Pending CN108553974A (en) | 2018-06-13 | 2018-06-13 | Filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108553974A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109806637A (en) * | 2019-03-20 | 2019-05-28 | 广东职业技术学院 | A kind of filter for textile dyeing |
| CN112279473A (en) * | 2020-05-13 | 2021-01-29 | 河海大学 | Continuous reactor for dissolving, separating and dehydrating sludge by using liquid dimethyl ether |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203624567U (en) * | 2013-12-09 | 2014-06-04 | 东江环保股份有限公司 | Spiral conveying type vacuum filtration washing machine |
| CN204182190U (en) * | 2014-10-30 | 2015-03-04 | 蒋央芳 | A kind of sand filtration washing drying integral machine |
| CN207237414U (en) * | 2017-08-25 | 2018-04-17 | 东营安诺其纺织材料有限公司 | Automatic filtering machine |
| CN208406241U (en) * | 2018-06-13 | 2019-01-22 | 长沙鑫本药业有限公司 | filter |
-
2018
- 2018-06-13 CN CN201810604131.9A patent/CN108553974A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203624567U (en) * | 2013-12-09 | 2014-06-04 | 东江环保股份有限公司 | Spiral conveying type vacuum filtration washing machine |
| CN204182190U (en) * | 2014-10-30 | 2015-03-04 | 蒋央芳 | A kind of sand filtration washing drying integral machine |
| CN207237414U (en) * | 2017-08-25 | 2018-04-17 | 东营安诺其纺织材料有限公司 | Automatic filtering machine |
| CN208406241U (en) * | 2018-06-13 | 2019-01-22 | 长沙鑫本药业有限公司 | filter |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109806637A (en) * | 2019-03-20 | 2019-05-28 | 广东职业技术学院 | A kind of filter for textile dyeing |
| CN112279473A (en) * | 2020-05-13 | 2021-01-29 | 河海大学 | Continuous reactor for dissolving, separating and dehydrating sludge by using liquid dimethyl ether |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |