CN204474478U - A kind of production water for pharmaceutical purposes device - Google Patents
A kind of production water for pharmaceutical purposes device Download PDFInfo
- Publication number
- CN204474478U CN204474478U CN201420395956.1U CN201420395956U CN204474478U CN 204474478 U CN204474478 U CN 204474478U CN 201420395956 U CN201420395956 U CN 201420395956U CN 204474478 U CN204474478 U CN 204474478U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- water
- level
- filter
- pharmaceutical purposes
- 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
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 48
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 28
- 238000009826 distribution Methods 0.000 claims abstract description 22
- 239000012528 membrane Substances 0.000 claims abstract description 18
- 238000009928 pasteurization Methods 0.000 claims abstract description 9
- 238000003860 storage Methods 0.000 claims abstract description 8
- 230000001954 sterilising Effects 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical group [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 claims description 3
- 239000006004 Quartz sand Substances 0.000 claims description 2
- 230000000844 anti-bacterial Effects 0.000 claims description 2
- 230000001580 bacterial Effects 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 1
- 235000011089 carbon dioxide Nutrition 0.000 claims 1
- 230000003373 anti-fouling Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000003245 working Effects 0.000 description 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 229910001425 magnesium ion Inorganic materials 0.000 description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 229960003563 Calcium Carbonate Drugs 0.000 description 1
- 230000000274 adsorptive Effects 0.000 description 1
- 239000012523 bacterial endotoxin Substances 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drugs Drugs 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- -1 iron ion Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000414 obstructive Effects 0.000 description 1
- 238000005325 percolation Methods 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000008227 sterile water for injection Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 239000008215 water for injection Substances 0.000 description 1
Abstract
The utility model discloses a kind of production water for pharmaceutical purposes device, it is characterized in that comprising: pretreatment unit, reverse osmosis unit and storage distribution device three parts.Wherein pretreatment unit comprises: raw water box 1, raw water pump 2, pasteurization cabinet 3, more medium filter 4, activated charcoal filter 5 and accurate filter 6; Reverse osmosis unit comprises: one-level RO membrane reverse osmosis device 7 and EDI second level reverse osmosis apparatus 13; Storage distribution device comprises: pure water tank 15, distribution device 16 and with some a pipe network device 17.The utility model ensure that the effluent quality of water for pharmaceutical purposes meets pharmaceutical standards, and overall system architecture is simple, and stable water outlet, antifouling property are good.
Description
Technical field
The utility model belongs to medical producing apparatus technical field, relates generally to a kind of production water for pharmaceutical purposes device.
Background technology
Water is that in drug manufacture, consumption is maximum, uses the widest a kind of raw material, for the production of the preparation of process and pharmaceutical preparation.Water for pharmaceutical purposes is divided into purified water, water for injection and sterilized water for injection because its scope used is different.The former water of water for pharmaceutical purposes is usually from tap water or the phreatic water of waters corporation's supply, and former water directly can not be used as preparation or the experimental water of preparation, need carry out purifying treatment to former water.At present, existing technique is when processing former water, and pretreatment system is in the process of filtering, backwash repeatedly need be carried out, in the process of backwash, because the particulate matter such as the silt in preprocessing process, dust are more, cause the number of times of backwash more, reduce the work-ing life of reverse osmosis membrane.The stable conductivity of original RO/RO reverse osmosis unit is in lower level all the time in addition.
Summary of the invention
(1) technical problem that will solve
For solving the problem, the utility model proposes a kind of mechanical filtration systems for water for pharmaceutical purposes process in early stage, the number of backwashes of more medium filter and activated charcoal filter can be reduced, extend the work-ing life of reverse osmosis membrane.And select RO/EDI system to replace RO/RO system, make conductivity value more stable.
(2) technical scheme
The utility model discloses a kind of production water for pharmaceutical purposes device, it is characterized in that comprising: pretreatment unit, reverse osmosis unit and storage distribution device three parts; Wherein pretreatment unit comprises: raw water box, raw water pump, pasteurization cabinet, more medium filter, activated charcoal filter and accurate filter; Described pasteurization cabinet be for more medium filter in pretreatment unit and activated charcoal filter before sterilizing unit; The weighting material of described more medium filter is quartz sand; The weighting material of activated charcoal filter is gac; The weighting material of accurate filter is the soften resin of sodium form; Reverse osmosis unit comprises: one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus; In described one-level RO membrane reverse osmosis device, heat exchanger and antiscaling device are housed; What described reverse osmosis unit adopted is RO/EDI system, makes it under high pressure carry out reverse-osmosis treated by high-pressure pump; Storage distribution device comprises: pure water tank, distribution device and with some a pipe network device; Connected by distributing pipe line between each described device.
Further, the fresh-water tank storing one-level fresh water is housed between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus.
Further, between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus, de-gassing vessel is housed.
Further, interchanger and ultraviolet sterilizing lamp are housed in described distribution system.The major function room of the interchanger in distribution system maintains system water temperature, and periodically carries out Systems Sterilizer or sterilizing, is generally placed on the end return pipe net of distribution system.
(3) beneficial effect
Compared with prior art, it has following beneficial effect to the utility model: the utility model ensure that the effluent quality of water for pharmaceutical purposes meets pharmaceutical standards, and overall system architecture is simple, and stable water outlet, antifouling property are good.The utility model also proposes a kind of mechanical filtration systems for water for pharmaceutical purposes process in early stage, can reduce the number of backwashes of more medium filter and activated charcoal filter, extend the work-ing life of reverse osmosis membrane.And select RO/EDI system to replace RO/RO system, make conductivity value more stable.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic block diagram of the present utility model.
Embodiment
The utility model discloses a kind of device producing water for pharmaceutical purposes, it is characterized in that comprising: pretreatment unit, reverse osmosis unit and storage distribution device three parts.Wherein pretreatment unit comprises: raw water box 1, raw water pump 2, pasteurization cabinet 3, more medium filter 4, activated charcoal filter 5 and accurate filter 6; Reverse osmosis unit comprises: one-level RO membrane reverse osmosis device 7 and EDI second level reverse osmosis apparatus 13; Storage distribution device comprises: pure water tank 15, distribution device 16 and with some a pipe network device 17.Nature tap water enters raw water box 1, is delivered to pasteurization cabinet 3, then enters more medium filter 4 successively, by activated charcoal filter 5 and accurate filter 6 by raw water pump 2; Then the water outlet of accurate filter 6 enters in first-stage reverse osmosis device 7 and second level reverse osmosis apparatus 13 successively, carries out reverse-osmosis treated, remove the salts substances in former water by high-pressure pump under the effect of high pressure; The water outlet of second level reverse osmosis apparatus 13 enters in pure water tank 15 and stores, and the pure water in last pure water tank 15 after process is dispensed to each water spot pipe network device 17 of pharmacy system again by distribution device 16.The utility model ensure that the effluent quality of water for pharmaceutical purposes meets pharmaceutical standards, and overall system architecture is simple, and stable water outlet, antifouling property are good.
Described pasteurization cabinet 3 be for more medium filter in pretreatment unit 4 and activated charcoal filter 5 before sterilizing unit; Pasteurization cabinet is that liquid heat is continued 30 minutes to 80 to 85 degrees Celsius, is used for killing causing disease, rotten or unwanted organism of fermentation, and bacterial endotoxin can be can be controlled in 5EU/ml, be a good water system of pre-treatment.
Further, the more medium filter 4 in described pretreatment unit is filled stone sand mostly, and its Main Function utilizes membrane filtration, permeation filtration and contact percolation effect, removes large granular impurity, suspended substance, colloid etc. in water; Activated charcoal filter 5 mainly by objectionable impuritiess such as the free chlorine in the adsorptive power removal water of activated carbon surface pore, microorganism, organism and part heavy metals, reaches the object of taste removal except look, impacts to prevent their low reverse osmosis membrane apparatus; Accurate filter 6 is mainly exchanged the calcium ion in water, magnesium ion by the soften resin of sodium form, thus filters out calcium ion and magnesium ion, removes the hardness in water.
Further, in described one-level RO membrane reverse osmosis device 7, heat exchanger 9 and antiscaling device 10 are housed; Optimal working temp due to reverse osmosis membrane is 25 DEG C, and its water production rate is maximum at this temperature, so utilize heat exchanger 9 heat to the water entering reverse osmosis or lower the temperature, regulates inflow temperature to remain on (25 ± 2) DEG C.Described antiscaling device 10 Main Function is the solvability relatively increasing scale forming matter in water, and to prevent the material such as calcium carbonate, calcium sulfate to the obstruction of film, it also can prevent iron ion from blocking film simultaneously.
Further, described reverse osmosis unit replaces original RO/RO system by RO/EDI system, and Main Function makes it under high pressure carry out reverse-osmosis treated by high-pressure pump, removes the salts substances in former water.
Further, the fresh-water tank 12 storing one-level fresh water is housed between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus.
Further, de-gassing vessel 11 is housed between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus, mainly
Be used for the reduction CO in water
2to 5-10mg/l, increase the possibility of bacterial load, the growth of anti-bacteria.
Further, in described distribution system 16, interchanger and ultraviolet sterilizing lamp are housed.The major function room of the interchanger in distribution system maintains system water temperature, and periodically carries out Systems Sterilizer or sterilizing, is generally placed on the end return pipe net of distribution system.
Claims (4)
1. produce a water for pharmaceutical purposes device, it is characterized in that comprising: pretreatment unit, reverse osmosis unit and storage distribution device three parts; Wherein pretreatment unit comprises: raw water box, raw water pump, pasteurization cabinet, more medium filter, activated charcoal filter and accurate filter; Described pasteurization cabinet be for more medium filter in pretreatment unit and activated charcoal filter before sterilizing unit; The weighting material of described more medium filter is quartz sand; The weighting material of activated charcoal filter is gac; The weighting material of accurate filter is the soften resin of sodium form; Reverse osmosis unit comprises: one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus; In described one-level RO membrane reverse osmosis device, heat exchanger and antiscaling device are housed; What described reverse osmosis unit adopted is RO/EDI system, makes it under high pressure carry out reverse-osmosis treated by high-pressure pump; Storage distribution device comprises: pure water tank, distribution device and use water spot pipe network device; Connected by distributing pipe line between each described device.
2. production water for pharmaceutical purposes device according to claim 1, is characterized in that: the fresh-water tank storing one-level fresh water is housed between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus.
3. production water for pharmaceutical purposes device according to claim 2, it is characterized in that, between one-level RO membrane reverse osmosis device and EDI second level reverse osmosis apparatus, de-gassing vessel is housed, the carbonic acid gas in water is mainly used to be reduced to 5-10mg/l, increase the possibility of bacterial load, the growth of anti-bacteria.
4. production water for pharmaceutical purposes device according to claim 1, it is characterized in that: interchanger and ultraviolet sterilizing lamp are housed in described distribution system, the major function room of the interchanger in distribution system maintains system water temperature, and periodically carry out Systems Sterilizer or sterilizing, be generally placed on the end return pipe net of distribution system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420395956.1U CN204474478U (en) | 2014-07-18 | 2014-07-18 | A kind of production water for pharmaceutical purposes device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420395956.1U CN204474478U (en) | 2014-07-18 | 2014-07-18 | A kind of production water for pharmaceutical purposes device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204474478U true CN204474478U (en) | 2015-07-15 |
Family
ID=53630281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420395956.1U Expired - Fee Related CN204474478U (en) | 2014-07-18 | 2014-07-18 | A kind of production water for pharmaceutical purposes device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204474478U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698779A (en) * | 2015-11-12 | 2017-05-24 | 江苏鑫东方环保设备科技有限公司 | Purified-water production process system |
| CN111573940A (en) * | 2020-04-07 | 2020-08-25 | 青岛奥利普自动化控制系统有限公司 | Water purification device for pharmacy |
-
2014
- 2014-07-18 CN CN201420395956.1U patent/CN204474478U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698779A (en) * | 2015-11-12 | 2017-05-24 | 江苏鑫东方环保设备科技有限公司 | Purified-water production process system |
| CN111573940A (en) * | 2020-04-07 | 2020-08-25 | 青岛奥利普自动化控制系统有限公司 | Water purification device for pharmacy |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170814 Address after: 1503 room 9, R & D building, No. 223005, Haikou Road, Huaian economic and Technological Development Zone, Jiangsu Patentee after: Jiangsu Jinnuo Pharmaceutical Equipment Co., Ltd. Address before: 223005 Overseas Students Pioneer Park, 9 Haikou Road, Huaian Economic Development Zone, Jiangsu, China Patentee before: Huaian Jin Nuo pharmaceutical equipment company limited |
|
| 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: 20150715 Termination date: 20170718 |