CN206695097U - A kind of steam condensate (SC) cyclic utilization system - Google Patents
A kind of steam condensate (SC) cyclic utilization system Download PDFInfo
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- CN206695097U CN206695097U CN201720463310.6U CN201720463310U CN206695097U CN 206695097 U CN206695097 U CN 206695097U CN 201720463310 U CN201720463310 U CN 201720463310U CN 206695097 U CN206695097 U CN 206695097U
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- steam
- cyclic utilization
- utilization system
- steam condensate
- condensate
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- 125000004122 cyclic group Chemical group 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 230000005494 condensation Effects 0.000 claims abstract description 20
- 238000009833 condensation Methods 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims description 34
- 238000001514 detection method Methods 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000012267 brine Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Steam condensate (SC) is collected by condensation water collection tank in the utility model steam condensate (SC) cyclic utilization system, automatically steam generating chamber is squeezed into during high level to be achieved, condensed water in steam generation room is heated by heat exchanger, because condensed water contains amount of heat, a small amount of steam only need to be supplemented can be by condensing water vapor, high steam is produced, is used for workshop steam using equipment, so steam condensate (SC) can be subjected to secondary cycle utilization.
Description
Technical field
Field of medicaments is the utility model is related to, particularly a kind of steam condensate (SC) cyclic utilization system.
Background technology
Steam is used on a large scale as one of production of raw medicine indispensability energy, and each steam point of use in workshop exists at present
Steam condensate (SC) can be all discharged after steam use.
The discharging modes of condensed water have two kinds in the prior art：One kind is to be discharged into waste water system after being condensed by condenser；
Another kind is to be discharged into circulation, is discharged into the steam condensate (SC) of circulation because heat is very high, can cause recirculated water water
Pond temperature rises sharply, and influences workshop and normally produces.Originally utilizable thermal source, by both discharging modes, all into " negative "
Energy, cause energy waste serious.
Utility model content
The utility model purpose is to provide a kind of steam condensate (SC) cyclic utilization system, can more fully utilized cold
The heat of condensate.
In order to achieve the above-mentioned advantages, a kind of steam condensate (SC) cyclic utilization system of the utility model offer, including steam generating chamber,
Heat exchanger, condensation water collection tank and steam use equipment, and the steam generating chamber connects with heat exchanger inside, described cold
The entrance of Condensed water collection tank is connected with the steam using the outlet of equipment, outlet and the steam of the condensation water collection tank
The entrance connection of room occurs, the venthole of the steam generating chamber is connected with the steam using the entrance of equipment, the condensation
There is pump between water collecting tank and the steam generating chamber.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, the steam condensate (SC) circulation profit
Also include gas-liquid separator and condenser with system, the liquid outlet of the heat exchanger and the gas-liquid separator, condenser are successively
Series connection.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, set in the condensation water collection tank
There is the first liquid level detection unit.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, the heat exchanger and the gas-liquid
There is discharge opeing electrically-controlled valve between separator.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, the heating agent entrance of the heat exchanger
With heating agent electrically-controlled valve.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, have in the steam generation room
Second liquid level detection unit.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, also have in the steam generation room
There are pressure sensing cell or temperature detecting unit.
In one embodiment of the utility model steam condensate (SC) cyclic utilization system, the first level sensing list
First, described pump, second liquid level detection unit, the discharge opeing electrically-controlled valve, the pressure sensing cell or temperature detecting unit,
The heating agent electrically-controlled valve is electrically connected with the controller.
Steam condensate (SC) is collected by condensation water collection tank in the utility model steam condensate (SC) cyclic utilization system, is treated
Steam generating chamber is squeezed into automatically when reaching high level, condensed water in steam generation room is heated by heat exchanger, due to cold
Condensate contains amount of heat, and need to only supplement a small amount of steam can produce high steam by condensing water vapor, be used for workshop steam
Equipment uses, and so steam condensate (SC) can be carried out into secondary cycle utilization.
Brief description of the drawings
Fig. 1 show the structural representation of the steam condensate (SC) cyclic utilization system of the utility model first embodiment.
Embodiment
Further to illustrate that the utility model is to reach the technological means and effect that predetermined purpose of utility model taken,
Below in conjunction with accompanying drawing and preferred embodiment, to according to the utility model proposes embodiment, structure, feature and its effect,
Describe in detail as after.
Fig. 1 show the structural representation of the steam condensate (SC) cyclic utilization system of the utility model first embodiment.Please
Referring to Fig. 1, the steam condensate (SC) cyclic utilization system of the present embodiment includes steam generating chamber 1, heat exchanger 2, condensation water collection tank
3rd, steam uses equipment 4, gas-liquid separator 5, condenser 6.
Steam generating chamber 1 connects with the inside of heat exchanger 2, and the entrance of condensation water collection tank 3 uses the outlet of equipment 4 with steam
Connection, the outlet of condensation water collection tank 3 are connected with the entrance of steam generating chamber 1, and venthole and the steam of steam generating chamber 1 use
The entrance connection of equipment 4, liquid outlet and gas-liquid separator 5, the condenser 6 of heat exchanger 2 are sequentially connected in series.
The first liquid level detection unit 31 is provided with condensation water collection tank 3, between condensation water collection tank 3 and steam generating chamber 1
With pump 310, there is discharge opeing electrically-controlled valve 210 between heat exchanger 2 and gas-liquid separator 5, the heating agent entrance of heat exchanger 2 has heating agent
Electrically-controlled valve 220, steam generating chamber 1 is interior to have the second liquid level detection unit 11, pressure sensing cell or temperature detecting unit 12, excellent
Choosing the first liquid level detection unit 31, pump 310, the second liquid level detection unit 11, discharge opeing electrically-controlled valve 210, pressure sensing cell or
Temperature detecting unit 12, heating agent electrically-controlled valve 220 are electrically connected with the controller (not shown).
The steam condensate (SC) cyclic utilization system course of work of the present utility model is：
Condensation water collection tank 3 collects workshop steam and uses steam condensate (SC) caused by equipment 4；
When the first liquid level that the first liquid level detection unit 31 is detected in condensation water collection tank 3 is higher than the first level set threshold
During value, controller controlling pump 310 works is pumped into steam generating chamber 1 until that the first liquid level detection unit 31 detects is cold by condensed water
The first liquid level in Condensed water collection tank 3 is less than the first level set threshold value；
When the second liquid level detection unit 11 detects that the second liquid level is higher than the second given threshold, controller control heating agent electricity
Control valve 220 is opened until the second liquid level detection unit 11 detects that the second liquid level is less than the second level set threshold value, thus may be used
So that condensed water is converted into steam by heat exchanger；
When pressure sensing cell or temperature detecting unit 12 detect that pressure or temperature are less than pressure given threshold or temperature
During given threshold, the aperture increase of controller control heating agent electrically-controlled valve 220, when pressure sensing cell or temperature detecting unit 12 detect
When being higher than pressure given threshold or temperature given threshold to pressure or temperature, the aperture of controller control heating agent electrically-controlled valve 220 reduces；
When the second liquid level detection unit 11 detects that the second liquid level is less than the second level set threshold value, controller control heat
Matchmaker's electrically-controlled valve 220 is closed and controls discharge opeing electrically-controlled valve 210 to open, condensed water by after gas-liquid separator 5 enter condenser 6 with
Waste water system is discharged into after recirculated water heat-shift.
In one embodiment of the present utility model, heating agent can be the steam of HTHP.
Steam condensate (SC) is collected by condensation water collection tank in the utility model, squeezes into steaming automatically during high level to be achieved
Room occurs for vapour, and condensed water in steam generation room is heated by heat exchanger, because condensed water contains amount of heat, only needs to mend
A small amount of steam is filled condensing water vapor can be produced high steam, be used using equipment for workshop steam, so can be by steam
Condensed water carries out secondary cycle utilization.
In one embodiment of the present utility model, the second liquid level arranges condensed water when being less than the second level set threshold value
Go out, this is due to that steam uses the condensed water that equipment is discharged to be not belonging to pure condensation often with chilled brine, recirculated water cross-reference
Water, the condensed water of residual is discharged so it is prevented that steam generating chamber or fouling of heat exchangers after condensed water fully evaporates.
More than, only it is preferred embodiment of the present utility model, not makees any formal limit to the utility model
System, although the utility model is disclosed above with preferred embodiment, but is not limited to the utility model, any to be familiar with sheet
Technical professional, do not departing from the range of technical solutions of the utility model, when the technology contents work using the disclosure above
Go out a little change or be modified to the equivalent embodiments of equivalent variations, as long as be without departing from the content of the technical scheme of the utility model, according to
Any simple modification, equivalent variations and the modification made according to the technical essence of the utility model to above example, still fall within
In the range of technical solutions of the utility model.
Claims (8)
1. a kind of steam condensate (SC) cyclic utilization system, it is characterised in that including steam generating chamber, heat exchanger, condensation water collection
Tank and steam use equipment, and the steam generating chamber inside the heat exchanger with connecting, the entrance of the condensation water collection tank
It is connected with the steam using the outlet of equipment, the outlet of the condensation water collection tank connects with the entrance of the steam generating chamber
Connect, the venthole of the steam generating chamber and the steam are connected using the entrance of equipment, the condensation water collection tank and described
There is pump between steam generating chamber.
2. steam condensate (SC) cyclic utilization system according to claim 1, it is characterised in that the steam condensate (SC) circulation
Also include gas-liquid separator and condenser using system, the liquid outlet of the heat exchanger and the gas-liquid separator, condenser according to
Secondary series connection.
3. steam condensate (SC) cyclic utilization system according to claim 2, it is characterised in that in the condensation water collection tank
Provided with the first liquid level detection unit.
4. steam condensate (SC) cyclic utilization system according to claim 3, it is characterised in that the heat exchanger and the gas
There is discharge opeing electrically-controlled valve between liquid/gas separator.
5. steam condensate (SC) cyclic utilization system according to claim 4, it is characterised in that the heating agent of the heat exchanger enters
Mouth has heating agent electrically-controlled valve.
6. steam condensate (SC) cyclic utilization system according to claim 5, it is characterised in that have in the steam generation room
There is the second liquid level detection unit.
7. steam condensate (SC) cyclic utilization system according to claim 6, it is characterised in that in the steam generation room also
With pressure sensing cell or temperature detecting unit.
8. steam condensate (SC) cyclic utilization system according to claim 7, it is characterised in that the first level sensing list
First, described pump, second liquid level detection unit, the discharge opeing electrically-controlled valve, the pressure sensing cell or temperature detecting unit,
The heating agent electrically-controlled valve is electrically connected with the controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720463310.6U CN206695097U (en) | 2017-04-28 | 2017-04-28 | A kind of steam condensate (SC) cyclic utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720463310.6U CN206695097U (en) | 2017-04-28 | 2017-04-28 | A kind of steam condensate (SC) cyclic utilization system |
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| Publication Number | Publication Date |
|---|---|
| CN206695097U true CN206695097U (en) | 2017-12-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720463310.6U Active CN206695097U (en) | 2017-04-28 | 2017-04-28 | A kind of steam condensate (SC) cyclic utilization system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114384942A (en) * | 2021-12-10 | 2022-04-22 | 镇江北新建材有限公司 | Condensed water liquid level control system, method and device and gypsum board production line |
-
2017
- 2017-04-28 CN CN201720463310.6U patent/CN206695097U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114384942A (en) * | 2021-12-10 | 2022-04-22 | 镇江北新建材有限公司 | Condensed water liquid level control system, method and device and gypsum board production line |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20181130 Address after: 317016 No. 7 Donghai Fifth Avenue, Duqiao Town Medical Park, Linhai City, Taizhou City, Zhejiang Province Co-patentee after: Zhejiang Huahai Pharmaceutical Co., Ltd. Patentee after: Zhejiang Huahai Zhicheng Pharmaceutical Co., Ltd. Co-patentee after: Universal Bailey biological medicine research and development (Shanghai) Co., Ltd. Address before: 317000 No. 7 Donghai Fifth Avenue, Duqiao Town Medical Park, Linhai City, Taizhou City, Zhejiang Province Co-patentee before: Zhejiang Huahai Pharmaceutical Co., Ltd. Patentee before: Zhejiang Huahai Zhicheng Pharmaceutical Co., Ltd. |
|
| TR01 | Transfer of patent right |