CN203255992U - Energy-saving vapour-pressure type distilled water preparation device - Google Patents
Energy-saving vapour-pressure type distilled water preparation device Download PDFInfo
- Publication number
- CN203255992U CN203255992U CN 201320277060 CN201320277060U CN203255992U CN 203255992 U CN203255992 U CN 203255992U CN 201320277060 CN201320277060 CN 201320277060 CN 201320277060 U CN201320277060 U CN 201320277060U CN 203255992 U CN203255992 U CN 203255992U
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- China
- Prior art keywords
- distilled water
- evaporating pot
- water
- outlet
- condenser
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- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 105
- 239000012153 distilled water Substances 0.000 title claims abstract description 47
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 238000001704 evaporation Methods 0.000 claims abstract description 61
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 239000003595 mist Substances 0.000 claims description 10
- 230000008020 evaporation Effects 0.000 claims description 9
- 239000012530 fluid Substances 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 238000004821 distillation Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000008213 purified water Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 229940079593 drug Drugs 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011194 good manufacturing practice Methods 0.000 description 3
- 238000003908 quality control method Methods 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002070 germicidal effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- 229940127557 pharmaceutical product Drugs 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010819 recyclable waste Substances 0.000 description 1
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Abstract
The utility model discloses an energy-saving vapour-pressure type distilled water preparation device which comprises a water pump, an evaporating pot, an electric heater, a condenser and an air compressor, wherein a water inlet of the water pump is connected with a purifying water pipe, and a water outlet of the water pump is connected with a pure water inlet formed in the bottom of the evaporating pot; the electric heater is used for heating and evaporating water, and the electric heater is arranged at the bottom inside the evaporating pot; the condenser is used for condensing vapour into distilled water, and the condenser is arranged in the middle inside the evaporating pot; an outlet of the air compressor is connected with the upper part inside the evaporating pot in a communicating way; a distilled water outlet used for guiding the water condensed by the condenser is arranged on the position, which corresponds to the position of the condenser, of the evaporating pot; a distilled water outlet of the evaporating pot is connected with a distilled water pipe. The energy-saving vapour-pressure type distilled water preparation device disclosed by the utility model realizes that the vapour is remained at high temperature for a long time about 45 minutes after being subjected to compressing, purifying and condensing processes by using a high-pressure gas, thereby ensuring that finally output distilled water is sterile without a heat source and produced distilled water can meet the requirement of pharmaceutical production quality management standard for one time.
Description
Technical field
The utility model relates to a kind of pharmaceutical purpose distilled water preparation facilities, relates in particular to a kind of energy saving pneumatic formula distilled water preparation facilities.
Background technology
Distilled water is widely used in pharmacy industry, especially large usage quantity in pharmaceutical products.Traditional distilled water preparation facilities adopts the mode of the first rear condensation of evaporation to prepare distilled water usually, but because its evaporation and condensation are all finished under condition of normal pressure, so the ratio of the condensation process after the evaporation faster, the time that at high temperature stops is shorter, and about 15-20 minute, so sterilization is not thorough in this process, in order to reach the requirement of Good Manufacturing Practice and Quality Control of Drug, to carry out germicidal treatment to the distilled water of output toward contact, increase operation, reduce efficient.
The utility model content
The purpose of this utility model provides a kind of energy the disposable energy saving pneumatic formula distilled water preparation facilities that reaches the Good Manufacturing Practice and Quality Control of Drug requirement with regard to being in order to address the above problem.
The utility model is achieved through the following technical solutions above-mentioned purpose:
Energy saving pneumatic formula distilled water preparation facilities described in the utility model comprises water pump, evaporating pot, electric heater, condenser and air compressor machine, the water-in of described water pump is connected with the purifying water pipe, the water outlet of described water pump is connected with the pure water entrance of described evaporating pot bottom, described electric heater is used for the water heating evaporation, described electric heater is installed on the bottom in the described evaporating pot, it is distilled water that described condenser is used for vapor condensation, described condenser is installed on the middle part in the described evaporating pot, top in the outlet of described air compressor machine and the described evaporating pot is connected, the position corresponding with described condenser is provided with the distilled water outlet of deriving for the water after the described condenser condenses on the described evaporating pot, and the distilled water outlet of described evaporating pot is connected with the distillation water pipe.
Particularly, described condenser is the coil pipe of in-built cold water.
Further, the top in the described evaporating pot is equipped with mist eliminator, and the outlet of described air compressor machine is connected with the entrance of described mist eliminator, and the interior top of the outlet of described mist eliminator and described evaporating pot communicates.
Be connected with external pipeline between the upper and lower in the described evaporating pot, the middle part of described pipeline is connected in series with fluid level controller; As preferably, described fluid level controller is the transparent tube that is provided with leakage fluid dram.
In order to improve pre-efficiency of utilization, between described water pump and the described purifying water pipe interchanger is installed, the distilled water outlet of described evaporating pot is connected and is connected with described distillation water pipe behind the described interchanger again.
Further, also be connected with separator tube between the distilled water outlet of described evaporating pot and the described interchanger, the middle part of described separator tube is connected with the distilled water outlet of described evaporating pot, and the top of described separator tube is provided with pneumatic outlet, and the lower end of described separator tube is connected with described interchanger.The pneumatic outlet of separator tube top is used for non-condensable gases is discharged.
In order to accelerate evaporation, and increase the alternative of evaporation mode, the position that is positioned at described electric heater next door in the described evaporating pot also is provided with steam heating tube, and the steam-in of described steam heating tube and condensation-water drain are located at respectively outside the described evaporating pot.
The beneficial effects of the utility model are:
The utility model makes steam after overdraft, purification, condensation process with high pressure gas, at high temperature the residence time is longer, about 45 minutes, can guarantee that the distilled water of last output is aseptic, without thermal source, the distilled water of producing once just can reach the requirement of Good Manufacturing Practice and Quality Control of Drug; Be used for the heating pure water by the recyclable waste heat of interchanger, thereby reduced the energy consumption of evaporation pure water, saved energy spending.
Description of drawings
Fig. 1 is the structural representation of energy saving pneumatic formula distilled water preparation facilities described in the utility model.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
As shown in Figure 1, energy saving pneumatic formula distilled water preparation facilities described in the utility model comprises interchanger 12, water pump 11, evaporating pot 4, electric heater 8, steam heating tube 9, condenser 13, separator tube 1 and air compressor machine 6, the water-in of water pump 11 is connected in series afterwards with interchanger 12 and is connected with purifying water pipe 15, the water outlet of water pump 11 is connected with the pure water entrance of evaporating pot 4 bottoms, electric heater 8 and steam heating tube 9 are used for the water heating evaporation, electric heater 8 and steam heating tube 9 are installed on the bottom in the evaporating pot 4, the steam-in of steam heating tube 9 (unmarked among the figure) and condensation-water drain 10 are located at respectively outside the evaporating pot 4, it is distilled water that condenser 13 is used for vapor condensation, condenser 13 is the coil pipe of in-built cold water, condenser 13 is installed on the middle part in the evaporating pot 4, top in the evaporating pot 4 is equipped with mist eliminator 3, the outlet of air compressor machine 6 is connected with the entrance of mist eliminator 3, top in the outlet of mist eliminator 3 and the evaporating pot 4 communicates, the position corresponding with condenser 13 is provided with the distilled water outlet (figure is unmarked) of deriving for condenser 13 condensed water on the evaporating pot 4, the distilled water outlet of evaporating pot 4 is connected with the middle part of separator tube 1, the top of separator tube 1 is provided with pneumatic outlet, the lower end of separator tube 1 is connected in series afterwards with interchanger 12 and is connected with distillation water pipe 14, and 14 in water pipe of distillation is connected to the distilled water entrance (unmarked among the figure) of pharmaceutical equipment.
As shown in Figure 1, be connected with external pipeline between the upper and lower in the evaporating pot 4, the middle part of this pipeline is connected in series with fluid level controller 2, and fluid level controller 2 is for being provided with the transparent tube of leakage fluid dram.Also show air-valve 5 and vent valve 7 on the airduct of air compressor machine 6 among Fig. 1.
As shown in Figure 1, during work, the purified water pipe 15 of purified water enters and carries out preliminary preheating in the interchanger 12, and the purified water after the preheating is pumped in the evaporating pot 4 by water pump 11, and under the effect of electric heater 8 and/or steam heating tube 9, purified water is evaporated to rapidly steam.Simultaneously, the high pressure gas that air compressor machine 6 produces enter the top in the evaporating pot 4 after mist eliminator 3 demists, the pressure and temperature of steam is all improved, and have better sterilization effect.Middle part in evaporating pot 4, steam liquefies under the effect of condenser 13, and the distilled water outlet of process evaporating pot 4 enters in the separator tube 1, the part non-condensable gases that wherein contains is discharged by the pneumatic outlet on separator tube 1 top, in the remaining liquid inflow heat exchanger 12, carry out being transported to distillation water pipe 14 after the heat exchange with purified water, be used for the pharmaceutical equipment pharmacy.
Claims (8)
1. energy saving pneumatic formula distilled water preparation facilities, it is characterized in that: comprise water pump, evaporating pot, electric heater, condenser and air compressor machine, the water-in of described water pump is connected with the purifying water pipe, the water outlet of described water pump is connected with the pure water entrance of described evaporating pot bottom, described electric heater is used for the water heating evaporation, described electric heater is installed on the bottom in the described evaporating pot, it is distilled water that described condenser is used for vapor condensation, described condenser is installed on the middle part in the described evaporating pot, top in the outlet of described air compressor machine and the described evaporating pot is connected, the position corresponding with described condenser is provided with the distilled water outlet of deriving for the water after the described condenser condenses on the described evaporating pot, and the distilled water outlet of described evaporating pot is connected with the distillation water pipe.
2. energy saving pneumatic formula distilled water preparation facilities according to claim 1, it is characterized in that: described condenser is the coil pipe of in-built cold water.
3. energy saving pneumatic formula distilled water preparation facilities according to claim 1 and 2, it is characterized in that: the top in the described evaporating pot is equipped with mist eliminator, the outlet of described air compressor machine is connected with the entrance of described mist eliminator, and the top in the outlet of described mist eliminator and the described evaporating pot communicates.
4. energy saving pneumatic formula distilled water preparation facilities according to claim 1 and 2 is characterized in that: be connected with external pipeline between the upper and lower in the described evaporating pot, the middle part of described pipeline is connected in series with fluid level controller.
5. energy saving pneumatic formula distilled water preparation facilities according to claim 4, it is characterized in that: described fluid level controller is the transparent tube that is provided with leakage fluid dram.
6. energy saving pneumatic formula distilled water preparation facilities according to claim 1 and 2, it is characterized in that: between described water pump and the described purifying water pipe interchanger is installed, the distilled water outlet of described evaporating pot is connected and is connected with described distillation water pipe behind the described interchanger again.
7. energy saving pneumatic formula distilled water preparation facilities according to claim 6, it is characterized in that: also be connected with separator tube between the distilled water outlet of described evaporating pot and the described interchanger, the middle part of described separator tube is connected with the distilled water outlet of described evaporating pot, the top of described separator tube is provided with pneumatic outlet, and the lower end of described separator tube is connected with described interchanger.
8. energy saving pneumatic formula distilled water preparation facilities according to claim 1 and 2, it is characterized in that: the position that is positioned at described electric heater next door in the described evaporating pot also is provided with steam heating tube, and the steam-in of described steam heating tube and condensation-water drain are located at respectively outside the described evaporating pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320277060 CN203255992U (en) | 2013-05-21 | 2013-05-21 | Energy-saving vapour-pressure type distilled water preparation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320277060 CN203255992U (en) | 2013-05-21 | 2013-05-21 | Energy-saving vapour-pressure type distilled water preparation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203255992U true CN203255992U (en) | 2013-10-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320277060 Expired - Fee Related CN203255992U (en) | 2013-05-21 | 2013-05-21 | Energy-saving vapour-pressure type distilled water preparation device |
Country Status (1)
| Country | Link |
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| CN (1) | CN203255992U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082376A (en) * | 2016-08-24 | 2016-11-09 | 全武 | A kind of distillation machine with heat recovery function |
-
2013
- 2013-05-21 CN CN 201320277060 patent/CN203255992U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082376A (en) * | 2016-08-24 | 2016-11-09 | 全武 | A kind of distillation machine with heat recovery function |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20180913 Granted publication date: 20131030 |
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| PP01 | Preservation of patent right | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20210913 Granted publication date: 20131030 |
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| PD01 | Discharge of preservation of patent | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20210913 Granted publication date: 20131030 |
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| PP01 | Preservation of patent right | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20230521 Granted publication date: 20131030 |
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| PD01 | Discharge of preservation of patent | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131030 |
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| CF01 | Termination of patent right due to non-payment of annual fee |