CN202203916U - Device for producing pure vapor by using injection water - Google Patents
Device for producing pure vapor by using injection water Download PDFInfo
- Publication number
- CN202203916U CN202203916U CN2011202227242U CN201120222724U CN202203916U CN 202203916 U CN202203916 U CN 202203916U CN 2011202227242 U CN2011202227242 U CN 2011202227242U CN 201120222724 U CN201120222724 U CN 201120222724U CN 202203916 U CN202203916 U CN 202203916U
- Authority
- CN
- China
- Prior art keywords
- preheater
- evaporimeter
- water
- injection
- outlet
- 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 - Lifetime
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 126
- 238000002347 injection Methods 0.000 title abstract description 21
- 239000007924 injection Substances 0.000 title abstract description 21
- 239000002994 raw material Substances 0.000 claims description 35
- 239000008215 water for injection Substances 0.000 claims description 32
- 239000010865 sewage Substances 0.000 claims description 12
- 239000011148 porous material Substances 0.000 claims description 4
- 101100293261 Mus musculus Naa15 gene Proteins 0.000 claims 1
- 238000001704 evaporation Methods 0.000 abstract description 14
- 238000000926 separation method Methods 0.000 abstract description 7
- 230000008020 evaporation Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 8
- 238000010276 construction Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 235000014171 carbonated beverage Nutrition 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
Images
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a device for producing pure vapor by using injection water. The device is characterized by comprising a raw water tank, a raw water pump, a preheater, an evaporator, a vapor inlet flange, a condensed water outlet flange, an injection water inlet, an industrial vapor inlet, a pure vapor outlet, a condensed water outlet and a drain outlet, wherein the raw water tank is connected with the injection water inlet through a pipeline; the raw water pump is connected and arranged between the bottom of the raw water tank and the upper part of the preheater through a pipeline; the upper part of the evaporator is connected with the industrial vapor inlet through a pipeline; a barrel of the evaporator is connected with a barrel of the preheater through a pipeline; an injection water outlet on the lower part of the preheater is connected with the upper part of the evaporator through a pipeline; and the lower part of the evaporator is connected with the pure vapor outlet, the drain outlet and the top of the raw water tank through a pipeline respectively. The device has the advantages that: the pure vapor is produced by evaporating the injection water, industrial vapor enters the evaporator and the preheater to heat raw water at the same time, and unevaporated raw water enters the raw water tank for reutilization. Qualified pure vapor can be directly produced without a vapor-water separation device.
Description
Technical field
The utility model relates to a kind of device of producing pure steam; Relate in particular to a kind of device of producing pure steam with water for injection; Be specially adapted to the pure steam sterilizing of pharmacy, food, cosmetic industry, belong to the technology for producing field of pure steam.
Background technology
The existing employed raw water of pure steam generator all is a purified water, must meet the pure steam that pharmacopeia requires through producing carbonated drink separation after the purified water evaporation.The water separator of known pure steamer generator mainly contains king bolt isolating construction, three grades of isolating constructions of inside spin and screen type low speed isolating construction.
King bolt isolating construction evaporimeter spiral plate gap is bigger, and the Q baffle plate can not thoroughly stop drip chamber with moisture film; Spiral plate gas speed is too high, and thermal friction is serious, and service life of equipment was difficult to above 8 years; The water distribution of the big pure vapour of specification is difficult to reach evenly, is easy to generate part and restrains dried wall phenomenon, and the big output of area descends on the contrary; Unavailable raw water is up to 15%.
Three grades of isolating construction inside spins of inside spin board diameter is little, and centrifugal force can not accelerate to perfect condition with the drop of rising entrainment with steam, does not reach the separating effect of expection; In moment operating pressure increase, under the centrifugal force increase situation, lower shoe and liquid level distance are near, very easily form vacuum, and drop is brought in the steam of rising, is difficult to separate, and worsens separation accuracy on the contrary; Because there is the carbonated drink sorting hole at the center of pipe bundle combinations parts, tubulation must distribute by hoop, and it is even that water-distributing device is difficult for reaching branch water, causes heat exchange area not to be utilized fully, and the main phenomenon appears in part tubulation, partial portion, and steam production descends.
Isolating construction is on-dismountable in a cavity with the evaporation tubulation, and when spiral plate received gas long-term corrosion destruction, the whole failure loss of evaporimeter was serious.
The porosity of screen type low speed isolating construction separation silk screen is the key that guarantees that raw water is supplied with continuously, and the operation of twining the silk screen tightness, the difficulty of increase technology.It is very big that the evaporimeter diameter must design, otherwise gas speed rising separating effect is poorer; The height of cylinder receives the restriction of user room height, separates in short-term, very influences separating effect.Separate when bad, can not produce qualified pure steam.
The water separator steam-water separation effect of known pure steamer generator is poor, especially flows into the heavy water of separating in the raw water again.Exist carbonated drink to separate halfway risk: if separating effect is bad, steam gets on the water band easily, and the pure quality of steam of producing like this is undesirable, when using underproof pure steam to sterilize, can pollute to system.
Summary of the invention
The utility model discloses a kind of device of producing pure steam with water for injection; Must meet the pure steam that pharmacopeia requires to solve in the prior art through producing carbonated drink separation after the purified water evaporation; Problems such as the water separator steam-water separation effect of pure steamer generator is poor, and separating effect is bad.
The utility model is characterized in that: comprise raw material water tank, raw material water pump, preheater, evaporimeter, steam inlet flange, condensate outlet(discharge) flange, water for injection inlet, industrial steam inlet, pure steam outlet, condensate outlet, sewage draining exit; Raw material water tank is connected with the water for injection suction line, and water for injection injects in the raw material water tank from the water for injection inlet; Pipeline is connected and installed the raw material water pump between raw material water tank bottom and the preheater top; Steam inlet, evaporimeter top is connected with the industrial steam suction line, and pipeline connects between the cylindrical shell of evaporimeter and the cylindrical shell of preheater; The preheater bottom has the water for injection outlet after the preheating, and water for injection outlet in preheater bottom is connected with the evaporimeter upper pipeline; The bottom of evaporimeter and preheater cylindrical shell is connected with the condensate outlet line; The evaporimeter bottom is connected with pure steam outlet, sewage draining exit, raw material water tank overhead line respectively.
When feed injection acquires a certain degree with the liquid level of water pot, open the raw material water pump, be transported to the feed injection water from preheater top and carry out preheating in the preheater; The feed injection water flows out from the bottom of preheater; Top through the feed injection water inflow evaporator of preheating; The part evaporation in the heat exchanger tube of evaporimeter of feed injection water becomes pure steam, and the pure steam of evaporation falls into down in the short tube with the raw water that the end evaporates fully, and pure steam is exported from pure vapour delivery outlet; The raw water that the end evaporates is back in the raw material water tank from the bottom of following short tube, evaporates utilization once more.Industrial steam gets in the cylindrical shell of evaporimeter from the industrial steam inlet; Evaporimeter heats with industrial steam, and the cylindrical shell of evaporimeter and the cylindrical shell of preheater are linked by pipe, after industrial steam gets into and heats in the evaporimeter; Industrial steam gets into preheater and carries out preheating; The condensate that the heating back produces is discharged from the bottom of evaporimeter and preheater cylindrical shell respectively, merges into a pipeline after the discharge, drains from the condensate outlet.The lowermost end of following short tube is provided with sewage draining exit, regularly discharging.
The utility model evaporimeter comprises end socket, cover flange, shell flange, cylindrical shell, heat exchanger tube, following short tube; The water for injection outlet of preheater bottom is connected with evaporimeter top end socket pipeline; Cover flange, shell flange are fastened together end socket and cylindrical shell; End socket is communicated with the heat exchanger tube pore; Heat exchanger tube is communicated with down short bobbin hole; Water for injection after the preheating injects evaporimeter, flows into down short tube through heat exchanger tube; Pipeline connects between the cylindrical shell of the cylindrical shell of evaporimeter and preheater 3; Industrial steam gets in the cylindrical shell of evaporimeter from the industrial steam inlet, by the preheating steam exchange heat pipe heating of industrial steam and preheater; The following short tube of evaporimeter is connected with pure steam outlet, sewage draining exit, raw material water tank overhead line respectively.
The utility model preheater, evaporation structure are identical.
With water for injection is that raw water is introduced in the raw material water tank, is transported to the shell of preheater by the raw material water pump, gets in the evaporimeter shell after the preheating again and evaporates, and the steam that the evaporation back produces is gone out by pure steam outlet.Industrial steam gets into evaporimeter and preheater simultaneously, the raw water in the heating tube side, and the raw water of end evaporation gets into recycling in the raw material water tank.The raw material water tank blowdown is regularly discharged.
The good effect of the utility model is: produces pure steam with the water for injection evaporation, need not water separator, and the qualified pure steam of ability Direct Production, easy to operate in the use, need not expensive automatic control.
Description of drawings
Fig. 1 is the utility model structural representation;
Among the figure: 1 raw material water tank; 2 raw material water pumps; 3 preheaters; 4 evaporimeters; 5 steam inlet flanges; 6 condensate outlet(discharge) flanges; The 4a end socket; The 4b cover flange; The 4c shell flange; The 4d cylindrical shell; The 4e heat exchanger tube; The short down tube of 4f; K1 water for injection inlet; K2 industrial steam inlet; The pure steam outlet of K3; The outlet of K4 condensate; The K5 sewage draining exit.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described in further detail.
An embodiment of the utility model is as shown in Figure 1:
The utility model comprises raw material water tank 1, raw material water pump 2, preheater 3, evaporimeter 4, steam inlet flange 5, condensate outlet(discharge) flange 6, water for injection inlet K1, industrial steam inlet K2, pure steam outlet K3, condensate outlet K4, sewage draining exit K5; Evaporimeter 4 comprises end socket 4a; Cover flange 4b; Shell flange 4c; Cylindrical shell 4d; Heat exchanger tube 4e; Following short tube 4f; Preheater 3 bottom water for injection outlets are connected with evaporimeter 4 top end socket 4a pipelines; Cover flange 4b, shell flange 4c are fastened together end socket 4a and cylindrical shell 4d; End socket 4a is communicated with heat exchanger tube 4e pore; Heat exchanger tube 4e is communicated with a following short tube 4f pore; Water for injection after the preheating injects evaporimeter 4, flows into down short tube 4f through heat exchanger tube 4e; Pipeline connects between the cylindrical shell 4d of evaporimeter 4 and the cylindrical shell of preheater 3; Preheater 3, evaporimeter 4 structures are identical.Industrial steam gets in the cylindrical shell 4d of evaporimeter 4 from industrial steam inlet K2, by the preheating steam exchange heat pipe 4e heating of industrial steam and preheater 3.The bottom of evaporimeter 4 and preheater 3 cylindrical shells is connected with condensate outlet K4 pipeline.Raw material water tank 1 is connected with water for injection inlet K1, and water for injection injects in the raw material water tank 1 from water for injection inlet K1; Pipeline is connected and installed raw material water pump 2 between raw material water tank 1 bottom and preheater 3 tops; Steam inlet, evaporimeter 4 top is connected with industrial steam inlet K2 pipeline, and pipeline connects between the cylindrical shell 4d of evaporimeter 4 and the cylindrical shell of preheater 3; Preheater 3 bottoms have the water for injection outlet after the preheating, and preheater 3 bottom water for injection outlets are connected with evaporimeter 4 upper pipeline; 4 times short tube 4f of evaporimeter are connected with pure steam outlet K3, sewage draining exit K5, raw material water tank 1 overhead line respectively; When feed injection acquires a certain degree with the liquid level of water pot, open raw material water pump 2, be transported to the feed injection water from preheater 3 tops and carry out preheating in the preheater 3; The feed injection water flows out from the bottom of preheater; Top through the feed injection water inflow evaporator 4 of preheating; The part evaporation in the heat exchanger tube 4e of evaporimeter of feed injection water becomes pure steam, and the pure steam of evaporation falls into down in the short tube 4f with the raw water that the end evaporates fully, and pure steam is exported from pure vapour delivery outlet K3; The raw water that the end evaporates is back in the raw material water tank 1 from the bottom of following short tube 4f, evaporates utilization once more.Industrial steam gets in the cylindrical shell 4d of evaporimeter 4 from industrial steam inlet K2; Evaporimeter 4 usefulness industrial steams heat, and the cylindrical shell 4d of evaporimeter 4 and the cylindrical shell of preheater 3 are linked by pipe, after industrial steam gets into and heats in the evaporimeter; Industrial steam gets into preheater and carries out preheating; The condensate that the heating back produces is discharged from the bottom of evaporimeter 4 and preheater 3 cylindrical shells respectively, merges into a pipeline after the discharge, and K4 drains from the condensate outlet.The lowermost end of following short tube 4f is provided with sewage draining exit K5, regularly discharging.
The course of work is following:
The utility model is raw water with water for injection; Water for injection injects in the raw material water tank 1 from water for injection inlet K1, when feed injection acquires a certain degree with the liquid level of water pot, and unlatching raw material water pump 2; Be transported to the feed injection water from preheater 3 tops and carry out preheating in the preheater 3; The feed injection water flows out from the bottom of preheater, and through the top of the feed injection water inflow evaporator 4 of preheating, the part evaporation in the heat exchanger tube 4e of evaporimeter of feed injection water becomes pure steam; The pure steam of evaporation falls into down in the short tube 4f with the raw water that the end evaporates fully; Pure steam is exported from pure vapour delivery outlet K3, and the raw water that the end evaporates is back in the raw material water tank 1 from the bottom of following short tube 4f, evaporates utilization once more.Industrial steam gets in the cylindrical shell 4d of evaporimeter 4 from industrial steam inlet K2; Evaporimeter 4 usefulness industrial steams heat, and the cylindrical shell 4d of evaporimeter 4 and the cylindrical shell of preheater 3 are linked by pipe, after industrial steam gets into and heats in the evaporimeter; Industrial steam gets into preheater and carries out preheating; The condensate that the heating back produces is discharged from the bottom of evaporimeter 4 and preheater 3 cylindrical shells respectively, merges into a pipeline after the discharge, and K4 drains from the condensate outlet.The lowermost end of following short tube 4f is provided with sewage draining exit K5, regularly discharging.
Claims (2)
1. produce the device of pure steam with water for injection for one kind, it is characterized in that: comprise raw material water tank, raw material water pump, preheater, evaporimeter, steam inlet flange, condensate outlet(discharge) flange, water for injection inlet, industrial steam inlet, pure steam outlet, condensate outlet, sewage draining exit; Raw material water tank is connected with the water for injection suction line; Pipeline is connected and installed the raw material water pump between raw material water tank bottom and the preheater top; Steam inlet, evaporimeter top is connected with the industrial steam suction line, and pipeline connects between the cylindrical shell of evaporimeter and the cylindrical shell of preheater; The preheater bottom has the water for injection outlet after the preheating, and water for injection outlet in preheater bottom is connected with the evaporimeter upper pipeline; The bottom of evaporimeter and preheater is connected with the condensate outlet line; The evaporimeter bottom is connected with pure steam outlet, sewage draining exit, raw material water tank overhead line respectively.
2. produce the device of pure steam according to claim 1 is described with water for injection, it is characterized in that: evaporimeter comprises end socket, cover flange, shell flange, cylindrical shell, heat exchanger tube, short tube down; The water for injection outlet of preheater bottom is connected with evaporimeter top end socket pipeline; Cover flange, shell flange are fastened together end socket and cylindrical shell; End socket is communicated with the heat exchanger tube pore; Heat exchanger tube is communicated with down short bobbin hole; Pipeline connects between the cylindrical shell of evaporimeter and the cylindrical shell of preheater; The bottom of evaporimeter and preheater cylindrical shell is connected with the condensate outlet line; The following short tube of evaporimeter is connected with pure steam outlet, sewage draining exit, raw material water tank overhead line respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202227242U CN202203916U (en) | 2011-06-28 | 2011-06-28 | Device for producing pure vapor by using injection water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202227242U CN202203916U (en) | 2011-06-28 | 2011-06-28 | Device for producing pure vapor by using injection water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202203916U true CN202203916U (en) | 2012-04-25 |
Family
ID=45968037
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202227242U Expired - Lifetime CN202203916U (en) | 2011-06-28 | 2011-06-28 | Device for producing pure vapor by using injection water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202203916U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104819447A (en) * | 2015-04-24 | 2015-08-05 | 刘素梅 | Clean steam generation device |
| CN108302516A (en) * | 2018-01-16 | 2018-07-20 | 中国科学院上海高等研究院 | A kind of segmented steam generator and its system |
| CN112963816A (en) * | 2021-02-26 | 2021-06-15 | 楚天华通医药设备有限公司 | Pure steam generating device and working method thereof |
-
2011
- 2011-06-28 CN CN2011202227242U patent/CN202203916U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104819447A (en) * | 2015-04-24 | 2015-08-05 | 刘素梅 | Clean steam generation device |
| CN108302516A (en) * | 2018-01-16 | 2018-07-20 | 中国科学院上海高等研究院 | A kind of segmented steam generator and its system |
| CN108302516B (en) * | 2018-01-16 | 2019-07-12 | 中国科学院上海高等研究院 | A kind of segmented steam generator and its system |
| CN112963816A (en) * | 2021-02-26 | 2021-06-15 | 楚天华通医药设备有限公司 | Pure steam generating device and working method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Jilin Huatong Pharmaceutical Equipment Co.,Ltd. Assignor: Ma Qinghua Contract record no.: 2013220000007 Denomination of utility model: Device for producing pure vapor by using injection water Granted publication date: 20120425 License type: Exclusive License Record date: 20130425 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| ASS | Succession or assignment of patent right |
Owner name: CHANGCHUN XINHUATONG PHARMACEUTICAL EQUIPMENT CO., Free format text: FORMER OWNER: MA QINGHUA Effective date: 20140623 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 130119 CHANGCHUN, JILIN PROVINCE TO: 130000 CHANGCHUN, JILIN PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20140623 Address after: Xincheng Street Jingyue Development Zone in Jilin province 130000 Changchun No. 6969 Patentee after: Watertown Pharmaceutical Equipment Co., Ltd Address before: 130119 Jilin province Changchun Jingyue Development Zone Xinli Town No. 6969 Patentee before: Ma Qinghua |
|
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 130000 No. 888 Huatong street, nine economic development zone, Changchun, Jilin Patentee after: Chutian Huatong Medical Equipment Co Ltd Address before: Xincheng Street Jingyue Development Zone in Jilin province 130000 Changchun No. 6969 Patentee before: Watertown Pharmaceutical Equipment Co., Ltd |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120425 |