CN103553232A - Method for producing pharmaceutical water - Google Patents
Method for producing pharmaceutical water Download PDFInfo
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- CN103553232A CN103553232A CN201310565061.8A CN201310565061A CN103553232A CN 103553232 A CN103553232 A CN 103553232A CN 201310565061 A CN201310565061 A CN 201310565061A CN 103553232 A CN103553232 A CN 103553232A
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- water
- reverse osmosis
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- pure water
- pharmaceutical purposes
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Abstract
The invention discloses a method for producing pharmaceutical water. The method comprises the following steps: firstly, orderly feeding raw water into a quartz sand filter, an activated carbon filter and a security filter, and orderly feeding the water discharged from the security filter into a primary reverse osmosis device and a secondary reverse osmosis device; carrying out reverse osmosis treatment under the effect of high pressure, and removing salt materials in the raw water; feeding the water discharged from the secondary reverse osmosis device into a pure water tank to store; and finally transporting the pure water processed in the pure water tank to each water point of a pharmaceutical system. By adopting the method disclosed by the invention, the condition that the effluent quality of the pharmaceutical water accords with the pharmaceutical standard is ensured; the system is simple in overall structure, stable in effluent and good in antifouling property.
Description
Technical field
The present invention relates to medicine and manufacture field, specifically a kind of method of producing water for pharmaceutical purposes.
Background technology
Water is a kind of raw material that in drug manufacture, consumption is maximum, use is the widest, for the production of the preparation of process and pharmaceutical preparation.In the process water and testing process thereof of medicine manufacturing processed different steps, water is most popular material, raw material or starting material.The different modes of administration of medicine, has determined the different mass level requirements of water.Process water and laboratory water for medicine manufacturing processed different steps all need to meet requirement separately.In whole processing, storage and distribution process, the quality control of water is the focus that people pay close attention to.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of method of producing water for pharmaceutical purposes, guaranteed that the effluent quality of water for pharmaceutical purposes meets pharmaceutical standards, and entire system is simple in structure, and stable water outlet, antifouling property are good.
Technical scheme of the present invention is:
A method of producing water for pharmaceutical purposes, includes following steps:
(1), first former water enter quartz filter, removes graininess dust, humus, starch, Mierocrystalline cellulose, bacterium and algae in former water;
(2), the water outlet of quartz filter enters activated charcoal filter, removes heterochromatic, peculiar smell, chlorine residue and partial organic substances in former water;
(3), the water outlet of activated charcoal filter enters cartridge filter, the part particulate matter that obstruction quartz filter, activated charcoal filter cause because of backwash;
(4), the water outlet of cartridge filter enters in first-stage reverse osmosis device and second level reverse osmosis apparatus successively, carries out reverse-osmosis treated under the effect of high pressure, removes the salts substances in former water;
(5), the water outlet of second level reverse osmosis apparatus enters in pure water tank and stores, what the pure water after processing in last pure water tank was delivered to pharmacy system again respectively uses water spot.
First described former water enter in raw water box and deposit, and then be delivered in quartz filter by raw water pump.
The dilute solution feed flow end of described first-stage reverse osmosis device and second level reverse osmosis apparatus is all connected with external fresh-water tank, and the dilute solution side of first-stage reverse osmosis device and second level reverse osmosis apparatus is connected with respectively for one-level high-pressure pump and the secondary high-pressure pump of reverse osmotic pressure are provided.
Between described first-stage reverse osmosis device and second level reverse osmosis apparatus, be connected with PH setting device.
The feed-water end of described pure water tank is provided with air respiratorresuscitator.
In described pure water tank, be provided with spherical spray equipment.
The water side of described pure water tank is connected with ultraviolet sterilizer.
Advantage of the present invention:
(1), the present invention adopts quartz filter, activated charcoal filter and cartridge filter to carry out pre-treatment to former water, guaranteed the influent quality of reverse osmosis unit, is conducive to carrying out smoothly of reverse osmosis;
(2), the present invention adopts reverse osmosis unit to carry out further purifying treatment to former water, by Impurity removals such as the mineral ion in former water, bacterium, virus, organism and colloids, thereby obtained higher-quality pure water;
(3), low, the stable water outlet of working pressure of the present invention, antifouling property are good;
(4), the last water outlet of the present invention further adopts ultra-violet sterilization, avoids secondary pollution;
(5), one-piece construction of the present invention is simple, reliable, easy accessibility, is convenient to clean and safeguard.
Accompanying drawing explanation
Fig. 1 is schema of the present invention.
Embodiment
A method of producing water for pharmaceutical purposes, includes following steps:
(1), first former water enter in raw water box 1 to deposit and (deposit former water, play a shock absorption, prevent the unstable of pipe network water supply, guarantee the water supply steady and continuous of whole system, guarantee is reliably provided also to each equipment long-term behaviour) simultaneously, and then be delivered in quartz filter 2 by raw water pump, remove graininess dust, humus, starch, Mierocrystalline cellulose, bacterium and algae in former water;
(2), the water outlet of quartz filter 2 enters activated charcoal filter 3, removes heterochromatic, peculiar smell, chlorine residue and partial organic substances in former water;
(3), the water outlet of activated charcoal filter 3 enters cartridge filter 4, stops quartz filter, activated charcoal filter because of the part particulate matter that backwash causes, and guarantees the water quality of reverse osmosis system water outlet;
(4), the water outlet of cartridge filter 4 enters in first-stage reverse osmosis device 5 and second level reverse osmosis apparatus 6 successively, carries out reverse-osmosis treated under the effect of high pressure, removes the salts substances in former water; Wherein, the dilute solution feed flow end of first-stage reverse osmosis device 5 and second level reverse osmosis apparatus 6 is all connected with external fresh-water tank 7; The dilute solution side of first-stage reverse osmosis device 5 and second level reverse osmosis apparatus 6 is connected with respectively for one-level high-pressure pump 8 and the secondary high-pressure pump 9 of reverse osmotic pressure are provided; Because most of salt is removed in first-stage reverse osmosis device, make water be slightly acidic, for guaranteeing effluent characteristics, between first-stage reverse osmosis device and second level reverse osmosis apparatus, connect PH setting device 10, add alkali adjusting water outlet pH value aobvious neutral;
(5), the water outlet of second level reverse osmosis apparatus 6 enters in pure water tank 11 and stores, the pure water after processing in last pure water tank 11 deliver to again pharmacy system each with water spot; Wherein, the feed-water end of pure water tank 11 is provided with air respiratorresuscitator, is provided with spherical spray equipment in pure water tank 11; The water side of pure water tank 11 is connected with ultraviolet sterilizer 12.
Table 1 is the water quality standard that the present invention processes rear pure water.
Table 1
Above content is only to technique example of the present invention and explanation; affiliated those skilled in the art make various modifications to described specific embodiment or supplement or adopt similar mode to substitute; only otherwise depart from the technique of invention or surmount this scope as defined in the claims, all should belong to protection scope of the present invention.
Claims (7)
1. a method of producing water for pharmaceutical purposes, is characterized in that: include following steps:
(1), first former water enter quartz filter, removes graininess dust, humus, starch, Mierocrystalline cellulose, bacterium and algae in former water;
(2), the water outlet of quartz filter enters activated charcoal filter, removes heterochromatic, peculiar smell, chlorine residue and partial organic substances in former water;
(3), the water outlet of activated charcoal filter enters cartridge filter, the part particulate matter that obstruction quartz filter, activated charcoal filter cause because of backwash;
(4), the water outlet of cartridge filter enters in first-stage reverse osmosis device and second level reverse osmosis apparatus successively, carries out reverse-osmosis treated under the effect of high pressure, removes the salts substances in former water;
(5), the water outlet of second level reverse osmosis apparatus enters in pure water tank and stores, what the pure water after processing in last pure water tank was delivered to pharmacy system again respectively uses water spot.
2. a kind of method of producing water for pharmaceutical purposes according to claim 1, is characterized in that: first described former water enter in raw water box and deposit, and then be delivered in quartz filter by raw water pump.
3. a kind of method of producing water for pharmaceutical purposes according to claim 1, it is characterized in that: the dilute solution feed flow end of described first-stage reverse osmosis device and second level reverse osmosis apparatus is all connected with external fresh-water tank, the dilute solution side of first-stage reverse osmosis device and second level reverse osmosis apparatus is connected with respectively for one-level high-pressure pump and the secondary high-pressure pump of reverse osmotic pressure are provided.
4. a kind of method of producing water for pharmaceutical purposes according to claim 1, is characterized in that: between described first-stage reverse osmosis device and second level reverse osmosis apparatus, be connected with PH setting device.
5. a kind of method of producing water for pharmaceutical purposes according to claim 1, is characterized in that: the feed-water end of described pure water tank is provided with air respiratorresuscitator.
6. a kind of method of producing water for pharmaceutical purposes according to claim 1, is characterized in that: in described pure water tank, be provided with spherical spray equipment.
7. a kind of method of producing water for pharmaceutical purposes according to claim 1, is characterized in that: the water side of described pure water tank is connected with ultraviolet sterilizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310565061.8A CN103553232A (en) | 2013-11-14 | 2013-11-14 | Method for producing pharmaceutical water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310565061.8A CN103553232A (en) | 2013-11-14 | 2013-11-14 | Method for producing pharmaceutical water |
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| Publication Number | Publication Date |
|---|---|
| CN103553232A true CN103553232A (en) | 2014-02-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310565061.8A Pending CN103553232A (en) | 2013-11-14 | 2013-11-14 | Method for producing pharmaceutical water |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104445686A (en) * | 2014-11-25 | 2015-03-25 | 成都威尔诺生物科技有限公司 | Automatically controlled water purification and circulation system |
| CN106365255A (en) * | 2016-09-29 | 2017-02-01 | 绍兴汇升技术转让服务有限公司 | RO membrane water purification system |
| CN108178401A (en) * | 2018-01-19 | 2018-06-19 | 林婧 | A kind of water purifying device with the sterilization of LED deep UVs |
| CN108947035A (en) * | 2018-08-27 | 2018-12-07 | 北京金峡超滤设备有限责任公司 | A kind of water for pharmaceutical purposes purification process |
| CN109665653A (en) * | 2018-12-23 | 2019-04-23 | 平顶山泰克斯特高级润滑油有限公司 | The preparation method of the overstable hydraulic transmission medium of coal field green |
| CN111777210A (en) * | 2020-07-23 | 2020-10-16 | 山东海益化工科技有限公司 | Special high-quality water treatment process for chemical production |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201367376Y (en) * | 2009-03-05 | 2009-12-23 | 杨海刚 | Full-automatic digital remote control water treatment device |
| CN202346800U (en) * | 2011-11-18 | 2012-07-25 | 广州市水天水处理设备有限公司 | Sterile pure water tank |
| CN202881035U (en) * | 2012-09-29 | 2013-04-17 | 东莞日之泉蒸馏水有限公司 | Production device for preparing distilled water by employing reverse osmosis desalination technology |
| CN203007069U (en) * | 2012-12-31 | 2013-06-19 | 中国人民解放军南京军区南京总医院 | Water treatment system for mobile shelter hospital |
-
2013
- 2013-11-14 CN CN201310565061.8A patent/CN103553232A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201367376Y (en) * | 2009-03-05 | 2009-12-23 | 杨海刚 | Full-automatic digital remote control water treatment device |
| CN202346800U (en) * | 2011-11-18 | 2012-07-25 | 广州市水天水处理设备有限公司 | Sterile pure water tank |
| CN202881035U (en) * | 2012-09-29 | 2013-04-17 | 东莞日之泉蒸馏水有限公司 | Production device for preparing distilled water by employing reverse osmosis desalination technology |
| CN203007069U (en) * | 2012-12-31 | 2013-06-19 | 中国人民解放军南京军区南京总医院 | Water treatment system for mobile shelter hospital |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104445686A (en) * | 2014-11-25 | 2015-03-25 | 成都威尔诺生物科技有限公司 | Automatically controlled water purification and circulation system |
| CN106365255A (en) * | 2016-09-29 | 2017-02-01 | 绍兴汇升技术转让服务有限公司 | RO membrane water purification system |
| CN108178401A (en) * | 2018-01-19 | 2018-06-19 | 林婧 | A kind of water purifying device with the sterilization of LED deep UVs |
| CN108947035A (en) * | 2018-08-27 | 2018-12-07 | 北京金峡超滤设备有限责任公司 | A kind of water for pharmaceutical purposes purification process |
| CN109665653A (en) * | 2018-12-23 | 2019-04-23 | 平顶山泰克斯特高级润滑油有限公司 | The preparation method of the overstable hydraulic transmission medium of coal field green |
| CN111777210A (en) * | 2020-07-23 | 2020-10-16 | 山东海益化工科技有限公司 | Special high-quality water treatment process for chemical production |
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Application publication date: 20140205 |