CN209386269U - A kind of secondary steam high pressure regenerating unit - Google Patents
A kind of secondary steam high pressure regenerating unit Download PDFInfo
- Publication number
- CN209386269U CN209386269U CN201920084521.8U CN201920084521U CN209386269U CN 209386269 U CN209386269 U CN 209386269U CN 201920084521 U CN201920084521 U CN 201920084521U CN 209386269 U CN209386269 U CN 209386269U
- Authority
- CN
- China
- Prior art keywords
- vapour
- liquid separator
- steam
- outlet
- perforated plate
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to steaming plant technical fields, in particular a kind of secondary steam high pressure regenerating unit, including the first vapour liquid separator, first vapour liquid separator is equipped with steam inlet end and outlet side, the outlet side of first vapour liquid separator is connected with gas compressor, the sidewall bottom of first vapour liquid separator is connected with discharge outlet, gas compressor is connected with vapour chamber, compression vapor inlet is equipped at the top of the lateral wall of vapour chamber, the outlet end of gas compressor is connect with compression vapor inlet, and the intracavitary two sides up and down of vapour are separately installed with upper perforated plate and lower perforated plate.The utility model is compressed by the secondary steam of recycling digesting apparatus discharge, improve its pressure and temperature, then clean regeneration steam return digesting apparatus recycling is generated after transferring heat to water, reduce the life steam consumption of digesting apparatus, the secondary steam of high efficiente callback digesting apparatus discharge, it generates clean regeneration steam and returns to digesting apparatus recycling, reduce the steam consumption of equipment, reduce the operating cost of equipment.
Description
Technical field
The utility model relates to steaming plant technical field, specially a kind of secondary steam high pressure regenerating unit.
Background technique
Food production much requires to carry out boiling using steam direct heating, and digestion process discharges a large amount of secondary steaming
Vapour causes the thermal efficiency of digesting apparatus very low；Contain the non-condensable gas such as air, volatilization gas in the secondary steam of discharge,
Droplet, water mist, oil, the impurity such as smell, cannot directly recycle.Some factories meeting recovery section converting heat is hot water for vehicle
Between clean or give worker have a bath, single recovery efficiency and utilization efficiency are all very low.
It nowadays, in process of production all can a large amount of secondary steaming especially with digesting technoloy in food processing enterprises
Vapour discharge.Because the secondary steam temperature of discharge is not high, it is difficult to recycle.Add in consideration of it, we provide a kind of secondary steam
Press regenerating unit.
Utility model content
The purpose of this utility model is to provide a kind of secondary steam high pressure regenerating units, to solve in above-mentioned background technique
It proposes that the secondary steam temperature of discharge is not high nowadays in food processing enterprises, is difficult the problem of recycling.
To achieve the above object, the utility model provides the following technical solutions:
A kind of secondary steam high pressure regenerating unit, including the first vapour liquid separator, first vapour liquid separator are provided with
Steam inlet end and outlet side, the outlet side of first vapour liquid separator are connected with gas compressor, first vapour-liquid point
Sidewall bottom from device is connected with discharge outlet, and the gas compressor is connected with vapour chamber, setting at the top of the lateral wall of the vapour chamber
There is compression vapor inlet, the outlet end of the gas compressor is connect with compression vapor inlet, and the intracavitary two sides up and down of the vapour are pacified respectively
Equipped with upper perforated plate and lower perforated plate, evaporation cavity is installed above the upper perforated plate, the bottom of the lower perforated plate is connected with bottom cavity, institute
The bottom for stating bottom cavity is connected with pipeline, and the top exterior walls of the evaporation cavity are connected with two root canal roads, wherein a pipeline is connected with benefit
Water valve, another pipeline are connected with the first regulating valve, and first regulating valve is connected with second far from the one end of the evaporation cavity
Vapour liquid separator, second vapour liquid separator are provided with drain pipe, are connected with the first drain valve on the drain pipe, and described
One drain valve is connected with water tank, the side of the water tank and bottom difference far from the one end of second vapour liquid separator
Pipeline is set, and the water tank bottom pipe is connected with water pump, and the water tank side ducts are connected with the second drain valve, described
The one end of second drain valve far from the water tank connects the discharge outlet by pipeline, and the water outlet of the water pump passes through pipeline
The bottom cavity bottom pipe is connected, and the water outlet of the water pump is connected with one way stop peturn valve；
Several uniform equidistant and arranged in parallel steam-generating banks are provided between the upper perforated plate and lower perforated plate.
Preferably, the sidewall bottom of first vapour liquid separator is additionally provided with exhaust outlet, connected on the exhaust outlet
There is the second regulating valve.
Preferably, the inner wall of the evaporation cavity is connected with first pressure sensor.
Preferably, being equipped with second pressure sensor on the inner sidewall of the vapour chamber.
Preferably, the inner wall of the bottom cavity is provided with liquid level sensor.
Preferably, being provided with liquidometer on the water tank.
Preferably, the intracavitary portion of vapour is additionally provided with deflector, the deflector is helical form, the every evaporation tube
Beam passes through the deflector.
Compared with prior art, the utility model has the beneficial effects that
1, this secondary steam high pressure regenerating unit is compressed by the secondary steam of recycling digesting apparatus discharge, improves it
Pressure and temperature generates clean regeneration steam return digesting apparatus recycling after then transferring heat to water, to drop
The life steam consumption of low digesting apparatus, the secondary steam of high efficiente callback digesting apparatus discharge.
2, this secondary steam high pressure regenerating unit generates clean regeneration steam and returns to digesting apparatus recycling, and reduction is set
Standby life steam consumption, reduces the operating cost of equipment.
Detailed description of the invention
Fig. 1 is the principles of the present invention structural schematic diagram；
Fig. 2 is the structural schematic diagram of the utility model vapour chamber；
Fig. 3 is the schematic diagram of the intracavitary part steam-generating bank installation of the utility model vapour；
Fig. 4 is the operation principle schematic diagram of the utility model various kinds of sensors；
Fig. 5 is the connection circuit diagram of the utility model pressure/liquid level sensor and single-chip microcontroller；
Fig. 6 is the control circuit schematic diagram of the utility model single-chip microcontroller and solenoid valve.
In figure: 1, the first vapour liquid separator；2, gas compressor；3, water compensating valve；4, first pressure sensor；5, it first adjusts
Save valve；6, the second vapour liquid separator；7, vapor inlet is compressed；8, evaporation cavity；9, upper perforated plate；10, deflector；11, vapour chamber；12, it steams
Hair tube bank；13, lower perforated plate；14, the first drain valve；15, second pressure sensor；16, water tank；17, the second regulating valve；18,
Exhaust outlet；19, liquid level sensor；20, bottom cavity；21, one way stop peturn valve；22, discharge outlet；23, water pump；24, the second drain valve；
25, liquidometer.
Specific embodiment
Below in conjunction with the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out clear, complete
Site preparation description, it is clear that the described embodiments are only a part of the embodiments of the utility model, instead of all the embodiments.
Based on the embodiments of the present invention, obtained by those of ordinary skill in the art without making creative efforts
Every other embodiment, fall within the protection scope of the utility model.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside",
The orientation or positional relationship of the instructions such as " clockwise ", " counterclockwise " be based on the orientation or positional relationship shown in the drawings, be only for
Convenient for description the utility model and simplify description, rather than the equipment of indication or suggestion meaning or element must have specifically
Orientation is constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
That be related to circuit and electronic component and module in the utility model is the prior art, those skilled in the art
Member may be implemented completely, be not necessarily to superfluous words, and the content of the utility model protection is not related to the improvement for software and method yet.
Please refer to Fig. 1-6, the utility model the following technical schemes are provided:
A kind of secondary steam high pressure regenerating unit, as shown in Figure 1-3, include the first vapour liquid separator 1, the first vapor-liquid separation
Device 1 is provided with steam inlet end and outlet side, and the outlet side of the first vapour liquid separator 1 is connected with gas compressor 2, the first vapour-liquid
The sidewall bottom of separator 1 is connected with discharge outlet 22, and gas compressor 2 is connected with vapour chamber 11, sets at the top of the lateral wall of vapour chamber 11
It is equipped with compression vapor inlet 7, the outlet end of gas compressor 2 is connect with compression vapor inlet 7, and two sides are installed respectively up and down in vapour chamber 11
There are upper perforated plate 9 and lower perforated plate 13, the top of upper perforated plate 9 is equipped with evaporation cavity 8, and the bottom of lower perforated plate 13 is connected with bottom cavity 20, bottom
The bottom of chamber 20 is connected with pipeline, and the top exterior walls of evaporation cavity 8 are connected with two root canal roads, wherein a pipeline is connected with water compensating valve 3,
Another pipeline is connected with the first regulating valve 5, and the first regulating valve 5 is connected with the second vapour liquid separator far from the one end of evaporation cavity 8
6, the second vapour liquid separator 6 is provided with drain pipe, the first drain valve 14 is connected on drain pipe, the first drain valve 14 is far from second
The one end of vapour liquid separator 6 is connected with water tank 16, and pipeline, 16 bottom of water tank is respectively set in the side and bottom of water tank 16
Portion's pipeline is connected with water pump 23, and 16 side ducts of water tank are connected with the second drain valve 24, and the second drain valve 24 is far from water tank
16 one end connects discharge outlet 22 by pipeline, and the water outlet of water pump 23 connects 20 bottom pipe of bottom cavity, and water pump by pipeline
23 water outlet is connected with one way stop peturn valve 21；
Several uniform equidistant and arranged in parallel steam-generating banks 12 are provided between upper perforated plate 9 and lower perforated plate 13.
Further, the sidewall bottom of the first vapour liquid separator 1 is additionally provided with exhaust outlet 18, and is connected on exhaust outlet 18
Two regulating valves 17, the exhaust outlet 18 of setting and the second regulating valve 17 can exclude non-condensable gas in vapour chamber 11.
Specifically, the inner wall of evaporation cavity 8 is connected with first pressure sensor 4.Second is equipped on the inner sidewall of vapour chamber 11
Pressure sensor 15.The inner wall of bottom cavity 20 is provided with liquid level sensor 19.
It is provided with liquidometer 25 on water tank 16, the moisture storage capacity of water tank 16 can be monitored.
Deflector 10 is additionally provided with inside vapour chamber 11, deflector 10 is helical form, and every steam-generating bank 12 passes through deflector
10, all there are a notches for every circle deflector 10 and 11 wall contact position of vapour chamber, it is therefore an objective to compression vapour rotation be allowed laterally to wash away evaporation
The outer wall of tube bank 12, and flow downward.
It is worth noting that as shown in Figure 4 and Figure 5, first pressure sensor 4, second pressure sensor 15 and liquid level pass
Sensor 19 is connected separately with AT89S52 single-chip microcontroller, and first pressure sensor 4, second pressure sensor 15 and liquid level sensor
19 output end passes through conducting wire and is electrically connected with the end pin P3.6 of AT89S52 single-chip microcontroller, the outlet side setting of gas compressor 2
There is solenoid valve, water compensating valve 3 and the first regulating valve 5 are also all made of solenoid valve, and first pressure sensor 4 passes through AT89S52 single-chip microcontroller
The first regulating valve 5 is connected, second pressure sensor connects the solenoid valve of 2 outlet side of gas compressor by AT89S52 single-chip microcontroller,
Hydrostatic sensor 19 connects water compensating valve 3 by AT89S52 single-chip microcontroller.
It is worth noting that, the first pressure sensor 4 and second pressure sensor 15 in the present embodiment are without tin core sense intelligence
The gas-pressure type pressure sensor of the model GZP160 of Semiconductor Co., Ltd's production, hydrostatic sensor 19 are produced using the said firm
Model GZP6101D variable frequency pump pressure sensor, in addition, first pressure sensor 4, second pressure sensor 15 with
And the support circuit that connect with AT89S52 single-chip microcontroller of hydrostatic sensor 19 and power module are provided by the producer.
Further, as shown in fig. 6, each AT89S52 single-chip microcontroller is respectively connected with driving circuit, driving circuit includes
S8050 triode, T1P122 multiple tube, 1N4001 diode, S8050 triode and T1P122 multiple tube also function to amplification electric current
Signal function enables solenoid valve effectively to work, and the input terminal of S8050 triode passes through 4.7K resistance and AT89S52 single-chip microcontroller
The electrical connection of the end pin P0.4, the output end of S8050 triode is electrically connected by 5.1K resistance and the input terminal of T1P122 multiple tube
It connects, and the output end of T1P122 multiple tube is serially connected with 1N4001 diode and solenoid valve respectively, 1N4001 diode plays protection
Solenoid valve and the service life effect for extending driving circuit.
The detailed process of the secondary steam high pressure regenerating unit of the utility model is as follows:
(1) secondary steam discharged initially enters the first vapour liquid separator 1 and carries out vapor-liquid separation, and the liquid that will be separated
Drop is drained, and the secondary steam after removing drop carries out compression heating through gas compressor 2 again, is then sent into from compression vapor inlet 7
To in vapour chamber 11.
(2) second pressure sensor 15 is provided on vapour chamber 11, the outlet side of gas compressor 2 is provided with solenoid valve, uses
In the quantity of steam that control gas compressor 2 exports.
(3) vapour chamber 11 is a cylinder, and both ends are closed by upper perforated plate 9 and lower perforated plate 13,9 upper perforated plates and 13 lower perforated plates pair
Title is provided with many circular holes, is used to the fixed steam-generating bank 12 of welded seal, is hollow structure inside steam-generating bank 12, and steam-generating bank
12 are connected with evaporation cavity 8 and bottom cavity 20.
(4) steam-generating bank 12 passes through deflector 10, and deflector 10 is helical form, every circle deflector and 11 wall contact position of vapour chamber
All there are a notches, it is therefore an objective to allow compression vapour rotation laterally to wash away the outer wall of steam-generating bank 12, and flow downward.
(5) compression vapour washes away 12 process of steam-generating bank, transfers heat to steam-generating bank 12, compresses inside vapour after heat release
Water vapor component condensation becomes drop constantly toward flowing down, and condensed water is deposited on lower perforated plate 13.
(6) discharge outlet 22 is arranged in the lower perforated plate of vapour chamber 11 and 13 junction, and condensed water is flowed out from discharge outlet 22, dredges by second
Enter water tank 16 after water valve 24.It needs first to open water compensating valve 3 when equipment just starts and passes through toward soft water, soft water is supplemented in evaporation cavity
Bottom cavity 20 is flowed downstream into the pipe of steam-generating bank 12, liquid level sensor 19 is provided in bottom cavity 20, after certain liquid level is arrived in water filling
Water compensating valve 3 is automatically closed.
(7) in the course of work, steam-generating bank 12 passes to the water in pipe after the heat transfer that pipe outer wall absorbs compression vapour,
Water temperature is gradually increasing, and is then vaporized into regeneration steam.
(8) regeneration steam rises out of pipe, and collects in evaporation cavity 8, is provided with first pressure sensor on evaporation cavity 8
4, the opening and closing of the first regulating valve 5 on steam pipe is exported for controlling evaporation cavity 8, guarantees the pressure of output steam.
(9) regeneration steam enters the progress steam-water separation of vapour liquid separator 6 after the first regulating valve 5, and what is finally obtained is full
Digesting apparatus is returned to regeneration steam to reuse.
(10) condensed water that vapour liquid separator 6 is separated is discharged into water tank 16 by the first drain valve 14.Water tank
Water in 16 is pumped into bottom cavity 20 as equipment by water pump 23 and runs moisturizing.
Basic principles, main features, and advantages of the present invention has been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Be only the utility model preference, be not intended to limit the utility model, do not departing from the spirit and scope of the utility model
Under the premise of, the utility model also has various changes and improvements, these changes and improvements both fall within claimed it is practical
In novel range.The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (7)
1. a kind of secondary steam high pressure regenerating unit, it is characterised in that: including the first vapour liquid separator (1), first vapour-liquid
Separator (1) is provided with steam inlet end and outlet side, and the outlet side of first vapour liquid separator (1) is connected with gas compression
The sidewall bottom of machine (2), first vapour liquid separator (1) is connected with discharge outlet (22), and the gas compressor (2) is connected with
The lateral wall top of vapour chamber (11), the vapour chamber (11) is provided with compression vapor inlet (7), the outlet of the gas compressor (2)
End is connect with compression vapor inlet (7), and two sides are separately installed with upper perforated plate (9) and lower perforated plate (13) up and down in the vapour chamber (11),
It is equipped with evaporation cavity (8) above the upper perforated plate (9), the bottom of the lower perforated plate (13) is connected with bottom cavity (20), the bottom
The bottom of chamber (20) is connected with pipeline, and the top exterior walls of the evaporation cavity (8) are connected with two root canal roads, wherein a pipeline is connected with
Water compensating valve (3), another pipeline are connected with the first regulating valve (5), and the one of first regulating valve (5) separate the evaporation cavity (8)
End is connected with the second vapour liquid separator (6), and second vapour liquid separator (6) is provided with drain pipe, is connected on the drain pipe
It is connected to the first drain valve (14), first drain valve (14) is connected with far from the one end of second vapour liquid separator (6)
Pipeline, water tank (16) the bottom pipe connection is respectively set in water tank (16), the side and bottom of the water tank (16)
Have water pump (23), water tank (16) side ducts are connected with the second drain valve (24), and second drain valve (24) is separate
One end of the water tank (16) is connected the discharge outlet (22) by pipeline, and the water outlet of the water pump (23) is connected by pipeline
The bottom cavity (20) bottom pipe is connect, and the water outlet of the water pump (23) is connected with one way stop peturn valve (21)；
Several uniform equidistant and arranged in parallel steam-generating banks (12) are provided between the upper perforated plate (9) and lower perforated plate (13).
2. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: first vapour liquid separator
(1) sidewall bottom is additionally provided with exhaust outlet (18), is connected with the second regulating valve (17) on the exhaust outlet (18).
3. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: the inner wall of the evaporation cavity (8)
It is connected with first pressure sensor (4).
4. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: the inner sidewall of the vapour chamber (11)
On second pressure sensor (15) are installed.
5. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: the inner wall of the bottom cavity (20) is set
It is equipped with liquid level sensor (19).
6. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: be arranged on the water tank (16)
There are liquidometer (25).
7. secondary steam high pressure regenerating unit according to claim 1, it is characterised in that: also set inside the vapour chamber (11)
It is equipped with deflector (10), the deflector (10) is helical form, and the every steam-generating bank (12) passes through the deflector (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920084521.8U CN209386269U (en) | 2019-01-18 | 2019-01-18 | A kind of secondary steam high pressure regenerating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920084521.8U CN209386269U (en) | 2019-01-18 | 2019-01-18 | A kind of secondary steam high pressure regenerating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209386269U true CN209386269U (en) | 2019-09-13 |
Family
ID=67853703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920084521.8U Expired - Fee Related CN209386269U (en) | 2019-01-18 | 2019-01-18 | A kind of secondary steam high pressure regenerating unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209386269U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114992614A (en) * | 2022-06-21 | 2022-09-02 | 佛山市丰川节能科技有限公司 | Steam regeneration device, system and method for waste gas recovery |
-
2019
- 2019-01-18 CN CN201920084521.8U patent/CN209386269U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114992614A (en) * | 2022-06-21 | 2022-09-02 | 佛山市丰川节能科技有限公司 | Steam regeneration device, system and method for waste gas recovery |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203836931U (en) | Centralized-packing closed type high temperature steam condensate water recovery system | |
| CN210448331U (en) | Vacuum oil filter | |
| CN208786121U (en) | A kind of string tower desulphurization system for rinsing demister using recycling filtrate water | |
| CN209386269U (en) | A kind of secondary steam high pressure regenerating unit | |
| CN219547430U (en) | Steam condensate water system | |
| CN216620708U (en) | Energy-saving system for efficiently recycling condensed water | |
| CN211158626U (en) | High-efficient single-effect evaporation process system | |
| CN210833099U (en) | High-temperature ultrahigh-pressure reheating waste heat power generation device | |
| CN114367121A (en) | Evaporation concentration system | |
| CN2932025Y (en) | Electrode type steam trap | |
| CN221527406U (en) | Condensed water negative pressure recovery system for corrugated board production line | |
| CN200948368Y (en) | Mircro-negative-pressure type and freezing type packing tower tail gas recovery device | |
| CN219023851U (en) | Tail gas steam-water separation recycling device for condensate water tank | |
| CN210645726U (en) | Vacuum pipeline ethanol recovery system | |
| CN203036733U (en) | Unpowered water and vapor separation energy-saving conveying device | |
| CN219454717U (en) | Vacuum exhaust condensation water-saving system of green mud filter | |
| CN212585231U (en) | Circulating water cooling system for grease deodorization vacuum unit | |
| CN117228765B (en) | Phosphoric acid waste liquid secondary concentration MVR evaporator | |
| CN216788835U (en) | System for prolonging service life of steam jet pump | |
| CN216667636U (en) | Stable in structure's steam manufacturing pipe | |
| CN211339414U (en) | Carbon dioxide elution device in liquefied natural gas production | |
| CN220708136U (en) | Tail gas pretreatment condenser | |
| CN216557885U (en) | Self-evaporation device with water suction pump | |
| CN209820020U (en) | Integrated gas rectification and purification device | |
| CN213841413U (en) | Spiral evaporative condenser |
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: 20190913 Termination date: 20220118 |