CN203569011U - Filtering device for urofollitropin production - Google Patents
Filtering device for urofollitropin production Download PDFInfo
- Publication number
- CN203569011U CN203569011U CN201320758955.4U CN201320758955U CN203569011U CN 203569011 U CN203569011 U CN 203569011U CN 201320758955 U CN201320758955 U CN 201320758955U CN 203569011 U CN203569011 U CN 203569011U
- Authority
- CN
- China
- Prior art keywords
- urofollitropin
- production
- filtering device
- filter
- urine
- 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
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a filtering device for urofollitropin production and belongs to the field of medicine production. The filtering device for urofollitropin production is characterized in that the filtering device comprises a storage tank of liquid to be filtered, a closed filter, a clean liquid storage tank, a liquid supply pump and a ceramic membrane micro-filter which are sequentially connected through a pipeline. Compared with the prior art, the filtering device for urofollitropin production has the advantages that the production cost is reduced and the urine quality is improved.
Description
Technical field
The utility model relates to a kind of drug production unit, particularly a kind of filtration unit being applicable in Urofollitropin production process.
Background technology
Urofollitropin is to extract purifying from menopausal women urine, and its activeconstituents is FSH, and FSH has the ovarian follicle of promotion and raises and the effect of growing.Its production stage is: by regulating pH value to alkalescence, after filtration, ultrafiltration obtains concentrated solution, then add organic solvent to obtain throw out raw material, dry sediment obtains Urofollitropin.
In the production technique of existing Urofollitropin, the filtration unit of its use is as shown in Figure 1: after filtrate tanks 1 precipitation, urine is pressed into plate-and-frame filter press 3 through infusion pump 2, through plate-and-frame filter press 3, filter, must clarify urine, enter clear liquid storage tank 4, then through infusion pump 5, enter subsequent processing 6 and carry out ultrafiltration.
When plate-and-frame filter press 3 filters, need to use thickening filter paper, filtering accuracy is between 10 μ m ~ 20 μ m, and filter paper is disposable use, and thickening filter paper price is 20 yuan/, and workshop processes a collection of urine conventionally needs 100, and cost is 2000 yuan.240 batches of urines of annual processing, about 480,000 yuan of filter paper consumption, production cost is high, and output cost performance is low.
Utility model content
Technical assignment of the present utility model is for above the deficiencies in the prior art, a kind of more cheap and better Urofollitropin production of filter effect filtration unit is provided, to improve menopausal women urine quality after filtering, reduce production costs, increase work efficiency, accomplish cleaner production requirement.
The technical scheme in the invention for solving the technical problem is: a kind of Urofollitropin production filtration unit, is characterized in that: what comprise that pipeline is linked in sequence treats filtrate tanks, hermetic filtering machine, clear liquid accumulator tank, infusion pump, microfiltration of ceramic membrane device.
Between above-mentioned hermetic filtering machine and described clear liquid accumulator tank, be connected cartridge filter.
Above-mentioned treat filtrate tanks and hermetic filtering machine between have infusion pump.
Compared with prior art, the utlity model has following outstanding beneficial effect:
1, reduced the cost of menopausal women urine filtering;
2, improved the menopausal women urine quality after filtering;
3, the clarification urine that the utility model is produced has extended the work-ing life of subsequent processing ultra-filtration membrane.
Accompanying drawing explanation
Fig. 1 is existing Urofollitropin plate-and-frame filter press filtration unit schematic diagram.
Fig. 2 is filtration unit schematic diagram of the present utility model.
Embodiment
Below in conjunction with specification drawings and specific embodiments, the utility model is further illustrated.
As shown in Figure 2, the utility model comprises that pipeline is linked in sequence treats filtrate tanks 7, hermetic filtering machine 9, cleaning liquor storage tank 11 and microfiltration of ceramic membrane device 13.
Described treat filtrate tanks 7 and hermetic filtering machine 9 between have infusion pump 8, between described cleaning liquor storage tank 11 and microfiltration of ceramic membrane device 13, have infusion pump 12.
Described hermetic filtering machine 9 is sealed shell of tank internal vertical placement of multiple layers filter net sheet, and the stainless (steel) wire that described filter net sheet is plurality of specifications filters by pressurization or vacuum, removes urine solid sediment, jelly etc., obtains clarifying urine.Described filter net sheet can be repeatedly used, and occurs can also repairing after breakage, consumes low.
The filtering element of described microfiltration of ceramic membrane device 13 is ceramic membrane.
In prior art, when plate-and-frame filter press 3 filters, need to use thickening filter paper, filtering accuracy is between 10 μ m ~ 20 μ m, filter paper is disposable use, thickening filter paper price is 20 yuan/, and workshop processes a collection of urine conventionally needs 100, and cost is 2000 yuan.240 batches of urines of annual processing, about 480,000 yuan of filter paper consumption, consumption in 5 years is 2,400,000 yuan.And in the utility model, adopt microfiltration of ceramic membrane device, and use ceramic membrane as filtering element, 5 square metres of its filtration areas, its filtering accuracy is 0.45 μ m, uses by cleaning, its flux can recover as before.These size ceramic membrane microfiltration device 13 prices are 250,000 yuan, and ceramic membrane work-ing life is 5 years.The two compares, and the utility model filtering accuracy is high, and output cost performance is high.And after precision is the ceramic membrane filter of 0.45 μ m after filtration, can effectively remove the impurity such as part bacterium in urine, colloid, it is nearly 20% that urine clarity improves, and can make extend 2～3 years the work-ing life of subsequent processing ultra-filtration membrane.
In prioritization scheme, be to improve filter effect, between hermetic filtering machine 9 and microfiltration of ceramic membrane device 13, be connected cartridge filter 10.Cartridge filter claims again accurate filter, and its object is to remove the above fine particles of turbidity 1 degree, meets the requirement of subsequent handling to water inlet.
Operating process is as follows: after filtrate tanks 7 precipitations, urine is pressed in hermetic filtering machine 9 through infusion pump 8, through hermetic filtering machine 9, tentatively filter, remove urine solid sediment, jelly etc., obtain clarifying urine, through cartridge filter 10, enter clear liquid storage tank 11, then by infusion pump 12, be pressed into microfiltration of ceramic membrane device 13, carry out micro-filtration, after micro-filtration, filtrate enters subsequent processing 14 and carries out ultrafiltration.
It should be noted that; particular of the present utility model have been described in detail the utility model; for a person skilled in the art, the various apparent change of in the situation that not deviating from spirit and scope of the present utility model, it being carried out is all within protection domain of the present utility model.
Claims (3)
1. a Urofollitropin production filtration unit, is characterized in that: what comprise that pipeline is linked in sequence treats filtrate tanks, hermetic filtering machine, clear liquid accumulator tank, infusion pump, microfiltration of ceramic membrane device.
2. Urofollitropin production filtration unit according to claim 1, is characterized in that: between described hermetic filtering machine and described clear liquid accumulator tank, be connected cartridge filter.
3. Urofollitropin production filtration unit according to claim 1, is characterized in that: described treat filtrate tanks and hermetic filtering machine between have infusion pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320758955.4U CN203569011U (en) | 2013-11-28 | 2013-11-28 | Filtering device for urofollitropin production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320758955.4U CN203569011U (en) | 2013-11-28 | 2013-11-28 | Filtering device for urofollitropin production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203569011U true CN203569011U (en) | 2014-04-30 |
Family
ID=50536755
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320758955.4U Expired - Fee Related CN203569011U (en) | 2013-11-28 | 2013-11-28 | Filtering device for urofollitropin production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203569011U (en) |
-
2013
- 2013-11-28 CN CN201320758955.4U patent/CN203569011U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103304621A (en) | Process for extracting high-purity tea saponin from camellia seed cakes | |
| CN203569011U (en) | Filtering device for urofollitropin production | |
| CN203353611U (en) | Soy sauce filtering system | |
| CN202951402U (en) | Lysine production device with fermentation liquor treatment | |
| CN205874262U (en) | Sour dragon in mother liquor middle ancient times acid recovery device of gu long | |
| CN202080970U (en) | Reverse osmosis treatment system with high recovery rate | |
| CN205011563U (en) | Gelatin production sewage treatment plant | |
| CN101434644A (en) | Novel method for efficiently extracting mycoprotein by microfiltration membrane | |
| CN201815143U (en) | Liquid medicine filtering device | |
| CN202751884U (en) | Membrane filtration filter system for sugar industry | |
| CN204865182U (en) | Glue solution filter equipment | |
| CN104973709A (en) | Device for water purification and classification | |
| CN205556784U (en) | Printed circuit board is sour, alkaline copper chloride etching waste liquor cyclic utilization device | |
| CN109607838A (en) | A kind of pendimethalin waste water triple effect evaporation desalter | |
| CN214552573U (en) | Ultrafiltration membrane concentration device for enzyme liquid | |
| CN204737815U (en) | Organic waste water desalination is received and is strained device | |
| CN219848988U (en) | Membrane filtration concentration device for itaconic acid | |
| CN203602423U (en) | Circular ultrafiltration device capable of decontaminating deeply | |
| CN203591649U (en) | Automatic filtering device for oil plants | |
| CN215711950U (en) | Water purification unit preliminary treatment automatically cleaning system | |
| CN203833930U (en) | Filter system of p-hydroxy phenylglycine | |
| CN202460290U (en) | System for processing sludge | |
| CN207918555U (en) | Two level water water purification machine | |
| CN203269939U (en) | Equipment for producing beta-amylase | |
| CN203159345U (en) | Concentration system of sterile solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20140430 Termination date: 20181128 |