CN201473756U - Steam condensate recovery unit - Google Patents
Steam condensate recovery unit Download PDFInfo
- Publication number
- CN201473756U CN201473756U CN2009203050187U CN200920305018U CN201473756U CN 201473756 U CN201473756 U CN 201473756U CN 2009203050187 U CN2009203050187 U CN 2009203050187U CN 200920305018 U CN200920305018 U CN 200920305018U CN 201473756 U CN201473756 U CN 201473756U
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- steam
- condensed water
- condensate
- steam trap
- back pressure
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- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a steam condensate recovery unit, which comprises a condensate temporary-storage separating bowl (1) and a back-pressure steam trap (2). One end of the condensate temporary-storage separating bowl (1) is connected with a steam-consuming production device (3). The other end of the condensate temporary-storage separating bowl (1) is connected with the water inlet of the back-pressure steam trap (2). The water outlet of the back-pressure steam trap (2) is connected with a condensate recover device (4). Since a lever mechanism is used to automatically control the steam and the steam is used as the power, the utility model has the advantages that the no power is used to recover the condensate, the high-efficiency automatic condensate recovery is effectively realized, the operation is safe, stable and reliable, the steam condensate recovery rate is high, the investment is small and the like.
Description
Technical field
The utility model relates to a kind of condensate water recovery device, particularly a kind of steam condensate recovering device that is used for dyeing.
Background technology
Printing and dyeing enterprise is in the process that continuity is produced, heat carrier steam will become condensed water in process of production in the drying cylinder, drain by steam trap, this condensed water is that the high temperature and high pressure steam condensation forms, hardness is low, and impurity is few, also has the characteristics of high temperature, be applicable to a lot of links that dyeing and finishing is produced, but it collects and all utilizes difficulty bigger.
Printing and dyeing enterprise adopts electric water pump or conventional float type steam trap to carry out the condensed water recovery of drying cylinder and drying room mostly at present.The method that electric water pump reclaims condensed water need be provided with jumbo water storage tank, occupies than large space, invests greatlyyer, and there are problems such as leakage, cavitation, repair rate height in pump operation.And when adopting float type steam trap to reclaim condensed water, because this steam trap internal volume is less, pipeline water amount is also little, so steam trap open frequency height, the mode of the direct unlatching of steam trap simultaneously can't be stopped exhaust steam hydrophobic the time fully, wastes comparatively serious.
The utility model content
Technical problem to be solved in the utility model is to provide a kind of reclamation of condensate water rate height, steam condensate recovering device that investment cost is little, thereby overcomes the deficiencies in the prior art.
For solving the problems of the technologies described above the technical solution of the utility model: steam condensate recovering device.Comprise that condensed water keeps in cylinder, back pressure type steam trap, an end of the temporary cylinder of described condensed water connects process steam equipment, and the other end connects the water inlet of back pressure type steam trap; The delivery port of back pressure type steam trap connects the condensed water reclaimer.
In the above-mentioned steam condensate recovering device, check-valves is installed in delivery port one side of described back pressure type steam trap.
In the aforesaid steam condensate recovering device, between described back pressure type steam trap and described check-valves, be equipped with and look handleless cup.
In the aforesaid steam condensate recovering device, between temporary cylinder of described condensed water and described condensed water reclaimer, by-passing valve is installed.
Beneficial effect: steam condensate recovering device of the present utility model uses lever machinery to control steam automatically dexterously, and is power with steam, has realized the automatic recovery of condensed water effectively.And adopt reuse nearby and concentrated reuse way of combining, select for use the back pressure type steam trap as core component, utilize steam pressure, with the Reuse of Condensate from Drying Cylinder direct reuse after the washing part in washing; And after not having the board Reuse of Condensate from Drying Cylinder centralized collection of washing part, then utilize constant pressure water supply system, the higher board of supply water quality requirement.Have following main feature:
1), the device lift can reach more than 5 meters, gives up the method that condensed water is received in traditional water blowback, thoroughly stops disadvantages such as leakage that pump operation brings, cavitation, repair rate height.
2), the device because of need not to use electric water pump, so need not jumbo water storage tank, saved accommodation space, the minimizing investment cost.
3), device moves unattended, safety, stable, reliable.When reclaiming high-quality condensed water, running gear is few in the system, the maintenance of minimizing equipment, power is all by steam pressure, accomplish the unpowered state that condensed water reclaims, guarantee the interlock of equipment and host work simultaneously, the pressure of dependence system self, condensed water can be transported to the height more than five meters, solve the transmitting power problem that reclaims condensed water.Its reclamation of condensate water rate height, investment cost is little, reasonable price, payoff period is short.Adopt the every group of recyclable high-quality soft water 1100Kg/h of drying room in this device back for common printing and dyeing enterprise, water temperature is about 95 degree, and average separate unit per hour can be saved 45 kilograms of steam, saves 280 kilograms of high-quality condensed waters, and monthly average is saved steam and is worth at 2500 yuan.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The utility model is described in further detail below in conjunction with drawings and Examples.
The specific embodiment
Embodiment.As shown in Figure 1, comprise that condensed water keeps in cylinder 1, back pressure type steam trap 2, one end of the temporary cylinder 1 of condensed water connects process steam equipment 3 by pipeline, the other end is by the water inlet of pipeline connection back pressure type steam trap 2, and back pressure type steam trap 2 adopts the energy-efficient back pressure type drain valve of Li Shi board CS45H-16/25LA of the West Lake, Hangzhou valve plants.Delivery port one side at back pressure type steam trap 2 is equipped with check-valves 5, and check-valves 5 connects condensed water reclaimer 4 by pipeline.Be equipped with between back pressure type steam trap 2 and check-valves 5 and look handleless cup 6, looking handleless cup 6 effect is the convenient mobility status of observing condensed water in the pipeline, and what guarantee to produce normally carries out.For preventing that back pressure type steam trap 2 from not influencing the recovery of condensed water when taking place to stop up, between temporary cylinder 1 of condensed water and condensed water reclaimer, by-passing valve 7 is installed, steam condensate (SC) can directly be delivered in the condensed water reclaimer 4 by this by-passing valve 7.
During work, process steam equipment 3 (drying cylinder) water outlet enters the temporary cylinder 1 of condensed water through piping, the temporary cylinder 1 of this condensed water can increase the reserves of condensed water, avoid the frequent unlatching of steam trap 2, the effect of its carbonated drink separation simultaneously also can be avoided overflowing of steam, when condensed water is stored into certain amount, and valve open in the steam trap 2, rely on the back pressure of steam in the drying cylinder, be delivered to condensed water reclaimer 4 with the condensed water discharge and by pipeline.
Embodiment of the present utility model is not limited to the foregoing description, all belongs within the protection domain of the present utility model in the various variations of making under the prerequisite that does not break away from the utility model aim.
Claims (4)
1. steam condensate recovering device, comprise that condensed water keeps in cylinder (1), back pressure type steam trap (2), it is characterized in that: the end that described condensed water is kept in cylinder (1) connects process steam equipment (3), and the other end connects the water inlet of back pressure type steam trap (2); The delivery port of back pressure type steam trap (2) connects condensed water reclaimer (4).
2. steam condensate recovering device according to claim 1 is characterized in that: delivery port one side at described back pressure type steam trap (2) is equipped with check-valves (5).
3. steam condensate recovering device according to claim 2 is characterized in that: be equipped with between described back pressure type steam trap (2) and described check-valves (5) and look handleless cup (6).
4. according to claim 1,2 or 3 described steam condensate recovering devices, it is characterized in that: between temporary cylinder (1) of described condensed water and described condensed water reclaimer, by-passing valve (7) is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203050187U CN201473756U (en) | 2009-06-25 | 2009-06-25 | Steam condensate recovery unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203050187U CN201473756U (en) | 2009-06-25 | 2009-06-25 | Steam condensate recovery unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201473756U true CN201473756U (en) | 2010-05-19 |
Family
ID=42410002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009203050187U Expired - Fee Related CN201473756U (en) | 2009-06-25 | 2009-06-25 | Steam condensate recovery unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201473756U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106440756A (en) * | 2016-10-25 | 2017-02-22 | 顾金华 | Steam cylinder electric control drainage device |
| CN113007146A (en) * | 2021-04-16 | 2021-06-22 | 中南大学 | Water pump steam-mixing super-cavitation-preventing and noise-reducing device |
-
2009
- 2009-06-25 CN CN2009203050187U patent/CN201473756U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106440756A (en) * | 2016-10-25 | 2017-02-22 | 顾金华 | Steam cylinder electric control drainage device |
| CN113007146A (en) * | 2021-04-16 | 2021-06-22 | 中南大学 | Water pump steam-mixing super-cavitation-preventing and noise-reducing device |
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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: 20100519 Termination date: 20160625 |