CN206235178U - A kind of steam condensate (SC) reclamation set - Google Patents
A kind of steam condensate (SC) reclamation set Download PDFInfo
- Publication number
- CN206235178U CN206235178U CN201621319147.8U CN201621319147U CN206235178U CN 206235178 U CN206235178 U CN 206235178U CN 201621319147 U CN201621319147 U CN 201621319147U CN 206235178 U CN206235178 U CN 206235178U
- Authority
- CN
- China
- Prior art keywords
- injector
- condensation water
- steam condensate
- collection tank
- vacuum cylinder
- 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 - Fee Related
Links
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a kind of steam condensate (SC) reclamation set, including condensation water collection tank, jet pump, injector and process water pond;Condensation water inlet, the low-pressure steam outlet for collecting steam condensate (SC) and the evacuation port for being arranged on bottom are provided with condensation water collection tank, exhaust-valve is installed on evacuation port, switch valve is installed on condensation water inlet;The injector is venturi type injector, and injector is provided with liquid-inlet, gas feed and liquid outlet;The import Joining Technology millpond of jet pump, the liquid-inlet of the outlet connection injector of jet pump, the gas feed of injector connects the low-pressure steam outlet of condensation water collection tank.The utility model is used as power source by the use of water by the negative pressure produced by injector, steam condensate (SC) is formed low-pressure steam, then low-pressure steam is drawn into injector, and mixed with injection with water, heating injection water, so as to the heat energy in steam condensate (SC) be reclaimed.
Description
Technical field
The utility model is related to a kind of steam condensate (SC) reclamation set.
Background technology
In chemical enterprise, because production needs, it is often necessary to substantial amounts of steam, and substantial amounts of steam is therefore produced to condense
Water, in this some vapor condensed water, except a small part can be in addition to direct reuse, most condensed water is that to be directly discharged into underground dirty
Grid, then into sewage treatment plant, this not only increases the pressure of sewage disposal, also wastes contained in condensed water
A large amount of heat energy so that the energy cost of enterprise further cannot be reduced effectively.
Utility model content
The purpose of this utility model is the device for providing heat energy in a kind of new reuse steam condensate (SC), to reduce enterprise
Energy consumption cost, specific technical scheme is as follows:
A kind of steam condensate (SC) reclamation set, including condensation water collection tank, jet pump, injector and process water pond;
Condensation water inlet, the low-pressure steam outlet for collecting steam condensate (SC) is provided with condensation water collection tank and bottom is arranged on
Evacuation port, is provided with exhaust-valve on evacuation port, and switch valve is provided with condensation water inlet;The injector is venturi type
Injector, injector is provided with liquid-inlet, gas feed and liquid outlet;The import Joining Technology millpond of jet pump, spray
The liquid-inlet of the outlet connection injector of pump is penetrated, the low-pressure steam of the gas feed connection condensation water collection tank of injector goes out
Mouthful.
Further, the injector includes vacuum cylinder, inserts vacuum cylinder from one end of vacuum cylinder along the axis of vacuum cylinder
The nozzle of inner chamber, the other end of vacuum cylinder is connected with mixing chamber, and one end that nozzle is located at outside vacuum cylinder forms the injector
Liquid-inlet, the gas feed of above-mentioned injector is formed with the side wall of vacuum cylinder, the mixing chamber is tapered, mixing chamber
Stub end connects vacuum cylinder, and the small head end of mixing chamber forms the liquid outlet of above-mentioned injector.
The injector of said structure when in use, after injection water enters through the liquid-inlet of injector, sprays from nozzle,
Negative pressure can be formed in vacuum cylinder, can make to produce negative pressure in the condensation water collection tank being connected in the gas feed of injector, by
Higher in the water temperature in condensation water collection tank, under certain negative pressure, condensed water can produce boiling, form substantial amounts of low pressure and steam
Vapour, these low-pressure steams can be drawn onto in injector in the presence of negative pressure, mixed with water with injection, so as to by injection water
Heating.
Further, the end of nozzle is provided with straight length.Being provided with for straight length forms stabilization beneficial to injection water
Liquid stream, reduces the generation of vortex, it is ensured that vacuum effect.
Further, the jet pump is that lift is the centrifugal water pump of 30-70 meter water columns.The water of 30-70 meter water column lifts
Pump ensure that the vacuum effect produced by injector.
Further, difference in height >=12 meter of the gas feed of the tank deck of the condensation water collection tank and injector, and injection
Height of the height of the gas feed of device higher than the tank deck of condensation water collection tank.Difference in height is set to >=12 meters, is in order to anti-
Only condensed water is taken directly in injector.
Further, the outer wrap of the condensation water collection tank has heat-insulation layer.With reduce condensed water heat energy to external diffusion.
Further, the liquid outlet of the injector is connected in process water pond.Can so be used with circulation use technology
Water in pond, makes the temperature of the water in process water pond improve as far as possible.
The utility model is used as power source by the use of water by the negative pressure produced by injector, steam condensate (SC) is formed low pressure
, then be drawn into low-pressure steam in injector by steam, and is mixed with injection with water, heats injection water, injection water
The process water, or boiler feed water of heating can be needed, steam condensate (SC) is extracted as a result of the mode of evaporation
In heat energy, it is to avoid the impurity that directly steam condensate (SC) is brought as process water or boiler feed water, as steam is cold
The evaporation of lime set, is not only able to recovery section heat energy, moreover it is possible to recovery section steam condensate (SC), reduces the pressure of sewage disposal,
Also reduce the energy cost of enterprise., it is necessary to first by reclamation of condensate water to condensation water collection before utility model works
Tank, operationally, it is necessary to the switch valve that will be condensed on water inlet is closed, to ensure the negative pressure of condensation water collection tank.
Brief description of the drawings
Fig. 1 is a kind of structural representation of embodiment of the present utility model.
Specific embodiment
Embodiment 1:
Refering to Fig. 1, a kind of steam condensate (SC) reclamation set, it includes condensation water collection tank 10, jet pump 20, injector 30
With process water pond 40;The condensation water inlet 11, low pressure for collecting steam condensate (SC) is provided with condensation water collection tank 10
Steam (vapor) outlet 12 and the evacuation port 15 for being arranged on bottom, are provided with exhaust-valve 16 on evacuation port 15, on condensation water inlet 11
Switch valve 13 is installed;The injector 30 is venturi type injector, and injector is provided with liquid-inlet 31, gas feed 32
With liquid outlet 34;The import Joining Technology millpond 40 of jet pump 20, the outlet 22 of jet pump 20 connects the liquid of injector 30
Body import 31, the low-pressure steam outlet 12 of the connection condensation water collection of gas feed 32 tank 10 of injector 30.In condensation water collection
The outer wrap of tank has heat-insulation layer 14.The liquid outlet of injector is connected in process water pond.
In the present embodiment, injector 30 includes vacuum cylinder 36, is inserted from one end of vacuum cylinder along the axis 38 of vacuum cylinder 36
Enter the nozzle 35 of the inner chamber of vacuum cylinder, the other end of vacuum cylinder is connected with mixing chamber 33, and nozzle 35 is located at outside vacuum cylinder
End forms the liquid-inlet 31 of the injector, and the gas feed 32 of above-mentioned injector is formed with the side wall of vacuum cylinder, described
Mixing chamber 33 is tapered, and the stub end connection vacuum cylinder 36 of mixing chamber 33, the small head end of mixing chamber 33 forms above-mentioned injector
Liquid outlet, straight length 37 is provided with the end of nozzle.
In the present embodiment, it is the centrifugal water pump of 30-70 meter water columns that jet pump uses lift.The gas feed of injector
Highly higher than condensation water collection tank tank deck height, and the gas feed of tank deck and the injector of condensation water collection tank height
>=12 meters of difference.
, it is necessary to steam condensate (SC) is collected into condensation water collection tank first before the present embodiment work, and in process water
There is enough water in pond, then close the switch valve 13 on condensation water collection tank, open jet pump, jet pump is by process water
Water in pond is squeezed into injector, when water sprays from the nozzle of injector, with the gas in vacuum chamber from the liquid of injector
Body import is discharged, and is returned in process water pond, is recycled.
Because the gas in vacuum chamber tails off, negative pressure is produced, while making in the condensation water collection tank that is connected with vacuum chamber
Negative pressure is produced, when the pressure for vaporization corresponding to the pressure in condensation water collection tank is reduced to the temperature of condensed water, condensed water is received
Condensed water in collection tank comes to life, and produces low-pressure steam, and these low pressure can neatly be injected pumping and enter, and is sprayed with from nozzle
The water for going out is mixed, because low-pressure steam contains substantial amounts of heat energy, so that the partial heat energy in condensed water is through low-pressure steam quilt
It is transferred in the water in process water pond, while also partial condensation liquid is also into the water in process water pond.
Water circulation in process water pond is squeezed into injector, until can not again by the condensed water in condensation water collection tank
Untill vaporization.It is of course also possible to certain negative pressure value is set, as soon as after the negative pressure in condensation water collection tank reaches setting value,
Stop energy recovery, the remaining water in condensation water collection tank is discharged from evacuation port, regathering new steam condensate (SC) carries out heat
Can reclaim.
Claims (7)
1. a kind of steam condensate (SC) reclamation set, it is characterised in that including condensation water collection tank, jet pump, injector and technique
Millpond;Be provided with condensation water collection tank for collect steam condensate (SC) condensation water inlet, low-pressure steam outlet and set
The evacuation port in bottom is put, exhaust-valve is installed on evacuation port, switch valve is installed on condensation water inlet;The injector
It is venturi type injector, injector is provided with liquid-inlet, gas feed and liquid outlet;The import Joining Technology of jet pump
Millpond, the liquid-inlet of the outlet connection injector of jet pump, the gas feed of injector connects the low of condensation water collection tank
Pressure steam (vapor) outlet.
2. steam condensate (SC) reclamation set according to claim 1, it is characterised in that the injector include vacuum cylinder,
The nozzle of the inner chamber of vacuum cylinder is inserted from one end of vacuum cylinder along the axis of vacuum cylinder, the other end of vacuum cylinder is connected with mixing
Room, one end that nozzle is located at outside vacuum cylinder forms the liquid-inlet of the injector, is formed with the side wall of vacuum cylinder above-mentioned
The gas feed of injector, the mixing chamber is tapered, and the stub end connection vacuum cylinder of mixing chamber, the small head end of mixing chamber is formed
The liquid outlet of above-mentioned injector.
3. steam condensate (SC) reclamation set according to claim 2, it is characterised in that the end of nozzle is provided with straight tube
Section.
4. steam condensate (SC) reclamation set according to claim 1, it is characterised in that the jet pump is that lift is 30-
The centrifugal water pump of 70 meter water columns.
5. steam condensate (SC) reclamation set according to claim 1, it is characterised in that the tank deck of the condensation water collection tank
With the tank that the height of difference in height >=12 meter of the gas feed of injector, and the gas feed of injector is higher than condensation water collection tank
The height on top.
6. steam condensate (SC) reclamation set according to claim 1, it is characterised in that the outside of the condensation water collection tank
It is enclosed with heat-insulation layer.
7. steam condensate (SC) reclamation set according to claim 1, it is characterised in that the liquid outlet of the injector connects
It is connected in process water pond.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621319147.8U CN206235178U (en) | 2016-12-02 | 2016-12-02 | A kind of steam condensate (SC) reclamation set |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621319147.8U CN206235178U (en) | 2016-12-02 | 2016-12-02 | A kind of steam condensate (SC) reclamation set |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206235178U true CN206235178U (en) | 2017-06-09 |
Family
ID=58977749
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621319147.8U Expired - Fee Related CN206235178U (en) | 2016-12-02 | 2016-12-02 | A kind of steam condensate (SC) reclamation set |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206235178U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109258219A (en) * | 2018-09-18 | 2019-01-25 | 河南师范大学 | A kind of efficient sunlight-heat reaources for wheat planting utilize device |
-
2016
- 2016-12-02 CN CN201621319147.8U patent/CN206235178U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109258219A (en) * | 2018-09-18 | 2019-01-25 | 河南师范大学 | A kind of efficient sunlight-heat reaources for wheat planting utilize device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN209242715U (en) | It is a kind of to prepare pure water system using waste heat multi-effect distilling | |
WO2017107020A1 (en) | Household solar seawater desalination apparatus | |
CN206235178U (en) | A kind of steam condensate (SC) reclamation set | |
CN201386995Y (en) | Condensed water flashing recycling device | |
CN204873907U (en) | Hot pressing formula distilled water machine system | |
CN205886510U (en) | System for non -methane total hydrocarbon waste gas content in reduction solution polymerization rubber technology | |
CN106517243B (en) | A kind of high temperature ammonia recycling device | |
CN202675929U (en) | Cooling device for improving vacuum effect of condenser | |
CN205973788U (en) | Regard as heat source to be used for device of hydrogen peroxide solution concentration production with steam heat pump | |
CN201818565U (en) | Heat pump with vacuum effect | |
CN201780001U (en) | Heating coil steam recoverer of waste heat power generation system | |
CN205402666U (en) | Can be with room that evaporates of steam waste heat recovery utilization | |
CN207699204U (en) | A kind of ammonium hydroxide preparation facilities | |
CN204494366U (en) | A kind of boiler blow down flash device steam recovery apparatus | |
CN207507035U (en) | A kind of recovery system of steam condensate (SC) | |
CN205744020U (en) | A kind of drain recovery case | |
CN209548763U (en) | Energy-saving dual-use traditional Chinese medicine extraction, concentrator | |
CN207850110U (en) | A kind of steam condensate recovering device | |
CN208292693U (en) | Biological heat energy coupled low temperature heat circulation evaporation process sewage recycles heat energy apparatus | |
CN203794732U (en) | Recycling device for recycling dimethylamine from wastewater | |
CN207295336U (en) | A kind of reclamation of condensate water reuse means | |
CN206113688U (en) | Dead steam recycling device | |
CN206613193U (en) | A kind of energy-saving multi-effect vapo(u)rization system | |
CN206184013U (en) | System for utilize air heat pump low temperature evaporative concentration alcohol waste liquid | |
CN205843134U (en) | A kind of vaporizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20170609 Termination date: 20191202 |