CN108841557A - The heating wine retort bottom pot system of recyclable waste heat - Google Patents
The heating wine retort bottom pot system of recyclable waste heat Download PDFInfo
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- CN108841557A CN108841557A CN201810969550.2A CN201810969550A CN108841557A CN 108841557 A CN108841557 A CN 108841557A CN 201810969550 A CN201810969550 A CN 201810969550A CN 108841557 A CN108841557 A CN 108841557A
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 42
- 235000014101 wine Nutrition 0.000 title claims abstract description 26
- 239000010819 recyclable waste Substances 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 101
- 239000002918 waste heat Substances 0.000 claims abstract description 65
- 238000011084 recovery Methods 0.000 claims abstract description 52
- 238000001704 evaporation Methods 0.000 claims abstract description 36
- 230000008020 evaporation Effects 0.000 claims abstract description 36
- 239000002912 waste gas Substances 0.000 claims abstract description 16
- 238000004064 recycling Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims description 83
- 239000000523 sample Substances 0.000 claims description 43
- 239000007789 gas Substances 0.000 claims description 25
- 238000001514 detection method Methods 0.000 claims description 12
- 239000003546 flue gas Substances 0.000 claims description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 10
- 230000005622 photoelectricity Effects 0.000 claims description 4
- 238000005086 pumping Methods 0.000 claims description 4
- 235000007164 Oryza sativa Nutrition 0.000 abstract description 7
- 238000004821 distillation Methods 0.000 abstract description 7
- 235000009566 rice Nutrition 0.000 abstract description 7
- 238000001816 cooling Methods 0.000 abstract description 4
- 240000007594 Oryza sativa Species 0.000 abstract 1
- 239000000498 cooling water Substances 0.000 description 10
- 230000001939 inductive effect Effects 0.000 description 10
- 239000013589 supplement Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- 241000209094 Oryza Species 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000000446 fuel Substances 0.000 description 6
- 238000009434 installation Methods 0.000 description 6
- 230000008901 benefit Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 230000009469 supplementation Effects 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 235000013339 cereals Nutrition 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 235000015096 spirit Nutrition 0.000 description 2
- 230000001502 supplementing effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
- 235000020097 white wine Nutrition 0.000 description 1
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Abstract
The present invention relates to brewed spirit equipment technical fields, more particularly to the heating wine retort bottom pot system of recyclable waste heat, it further include being installed on the intrinsic heat exchanger of bottom pot, the heat exchanger is connected to combustor and waste-heat recovery device respectively, the waste-heat recovery device is also connected to bottom pot ontology, and the waste-heat recovery device is also connected to transit joint circulation；The combustor is heated for heat exchanging device; the heat exchanger is for heating the intrinsic evaporation water of bottom pot; the waste-heat recovery device is recycled for waste-gas heat; the transit joint is for connecting heat exchanger entrance end and combustor outlet end; the more conventional distillation rice steamer bottom pot of the present apparatus; heat loss is small; the loss of energy is low; it can play the role of cooling protection connectivity port but also the heat of connectivity port is used for heating evaporation water; the function of the recycling of waste heat is reached, so that brewing cost be greatly saved.
Description
Technical field
The present invention relates to brewed spirit equipment technical field more particularly to the heating wine retort bottom pot systems of recyclable waste heat.
Background technique
In brewed spirit industry, white wine needs to separate from fermenting-ripening grain unstrained spirits by distillation, distills
Journey is a most link of liquor production energy consumption.Currently, being all to generate steaming by boiler in most of liquor-making enterprises
Vapour, then given by pipeline to distillation rice steamer bottom pot, white liquor distilling is realized by control steam pressure；Steam heating is because of boiler efficiency
The not high, reasons such as pipeline heat loss is big, energy consumption is higher, and the connectivity port of heat exchanger and combustor is easy to happen height
Temperature damage, increases the maintenance cost of boiler.
In conclusion needing the heating wine retort bottom pot system of recyclable waste heat at present.
Summary of the invention
In view of the above-mentioned problems, the purpose of the present invention is to provide the heating wine retort bottom pot systems of recyclable waste heat.
To achieve the above object, the technical solution adopted by the present invention is：
The heating wine retort bottom pot system of recyclable waste heat, including upper cover and bottom pot ontology, further include being installed on bottom pot ontology
Interior heat exchanger, the heat exchanger are connected to combustor and waste-heat recovery device respectively, the waste-heat recovery device also with bottom pot
Ontology connection, the waste-heat recovery device are also connected to transit joint circulation；The combustor is heated for heat exchanging device, described
Heat exchanger is recycled for heating the intrinsic evaporation water of bottom pot, the waste-heat recovery device for waste-gas heat, the transition
Connector is for connecting heat exchanger entrance end and combustor outlet end.
A certain amount of water is added in the pot ontology of bottom, keeps heat exchanger submerged in water, is added using burner heat exchanging device
Heat, the mode that the heat that heat exchanger generates leads to heat transfer is fully absorbed by the bottom intrinsic water of pot, and fuel is in heat exchanger
The high-temperature tail gas that middle burning generates enters waste-heat recovery device, heats to the water in waste-heat recovery device, waste heat recycling dress
It sets and is connected to bottom pot ontology, the water after heating can be used for supplementing evaporation water in the pot ontology of bottom, to greatly improve the present apparatus
The thermal efficiency, waste-heat recovery device are also connected to transit joint circulation, and transit joint is for connecting heat exchanger exit end and combustor
Arrival end, water flow are circulated along transit joint and waste-heat recovery device, can play the role of cooling protection connectivity port again
The high temperature heat of connectivity port can be used for the heating of cooling water, reached the function of the recycling of waste heat, the present apparatus is more normal
The distillation rice steamer bottom pot of rule, heat loss is small, and the loss of energy is low, can extend the service life of the connectivity port of heat exchanger and combustor,
To which brewing cost be greatly saved.
It preferably, further include having liquid level tube, the liquid level tube is connected to bottom pot ontology, and liquid level tube is connected to bottom pot ontology,
Under the action of water pressure, pot intrinsic water in bottom enters in liquid level tube, and bottom pot ontology and liquid level tube is made to keep identical liquid level,
By observing the liquid level of liquid level tube it can be learnt that the intrinsic water of bottom pot, consequently facilitating being automatically replenished in time into bottom pot ontology
Evaporation water, avoids in use since water is very few, heat exchanger is not totally submerged thermal loss caused by Yu Shuizhong.
Preferably, liquid level sensor is installed, the liquid level sensor includes top photoelectricity on the liquid level inside pipe wall
Probe, middle part photoelectric probe and lower part photoelectric probe, state liquid level sensor by control device respectively with waste-heat recovery device
Electromagnetic valve electrical connection on electromagnetic valve and combustor tracheae, it is electric signal that liquid level sensor, which is by the high-degree of conversion of liquid level,
Form is exported, and liquid level sensor can be used for detecting the water surface elevation in liquid level tube and then detect the intrinsic liquid level of bottom pot
Highly, liquid level sensor includes along the vertically arranged top photoelectric probe of liquid level inside pipe wall, middle part photoelectric probe and lower part photoelectricity
Probe, when liquid level declines in liquid level tube, when middle part photoelectric probe is not contacted with liquid level, middle part photoelectric probe receives inductive signal,
And electric signal is converted by liquid level sensor and is transferred to control device, control device controls the electromagnetic valve of waste-heat recovery device
It automatically opens, until when top photoelectric probe and liquid level contact, top photoelectric probe connects the intrinsic evaporation water of supplement bottom pot
Inductive signal is received, and electric signal is converted by liquid level sensor and is transferred to control device, control device controls electromagnetic valve certainly
It is dynamic to close, so that the process for being automatically replenished evaporation water from the pot ontology of trend bottom by waste-heat recovery device is realized, when waste heat returns
When in receiving apparatus without adding cooling water in time and cannot continue to supplement the bottom intrinsic evaporation water of pot, the present apparatus is being used
In the process, pot intrinsic evaporation in bottom is persistently reduced with water, when lower part, photoelectric probe is not contacted with liquid level, lower part photoelectric probe
Inductive signal is received, and electric signal is converted to by liquid level sensor and is transferred to control device, is controlled and is burnt by control device
Electromagnetic valve on machine tracheae is automatically closed, and stops combustor heat exchanging device and continues to heat, to avoid due in the pot ontology of bottom
Evaporation is very few with water, and the heat that heat exchanger generates cannot be taken away in time, and bottom pot ontology is caused to be damaged by high temperature.
Preferably, the transit joint is cavity structure, the combustor outlet end and heat exchanger entrance end respectively with mistake
It crosses connector to be detachably connected, pumping plant, water is installed on the pipeline that the transit joint and waste-heat recovery device are connected by circulation
Pump installation circulates in waste-heat recovery device and transit joint for water and provides power, and recirculated cooling water can take away heat exchange in time
High temperature heat at device arrival end and combustor outlet end position, has the function of that connectivity port is protected not damaged by high temperature, and
And cooling water also is heated using high temperature heat, and then realize the secondary use of high temperature heat, combustor outlet end and heat exchange
Device arrival end is detachably connected with transit joint respectively, can facilitate transit joint and combustor outlet end and heat exchanger entrance end
Installation and the replacement of transit joint.
Preferably, the heat exchanger include burning cavity and exhaust gas storage cavity, the burning cavity respectively with combustor
It is connected to exhaust gas storage cavity, air and fuel are pressed proper proportion mix and convert so that it is in combustion chamber by pre-mixing apparatus by combustor
Internal full combustion, the high-temp waste gas generated after burning can store cavity by exhaust gas and store discharge in time, avoid burning cavity
Interior exhaust gas discharge causes insecurity factor not in time, and exhaust gas storage cavity has guiding role, and bootable exhaust gas is along certain
Direction outlet is conducive to improve manual operation environment.
Preferably, the waste-heat recovery device includes sink and the flue gas leading that is installed in sink, the flue gas leading and useless
Gas stores cavity connection, and high-temp waste gas enters in flue gas leading along exhaust gas storage cavity, and flue gas leading is installed in sink, can be used for pair
Water in sink is heated, and is realized to the heat recovery in high-temp waste gas, the water after heating is being added in the pot ontology of bottom,
The secondary use of waste-gas heat is realized, to improve the heat utilization ratio of boiler.
Preferably, the waste-heat recovery device is installed on the top of bottom pot ontology, the bottom of the sink and bottom pot ontology
It is connected to using adapter tube, the bottom of sink is connected to bottom pot ontology using pipeline, and waste-heat recovery device is installed on the upper of bottom pot ontology
Side opens electromagnetic valve when requiring supplementation with the bottom intrinsic evaporation water of pot, is pacified by waste-heat recovery device and bottom pot ontology
The hydraulic pressure effect that the difference in height of holding position generates automatically flows into water in the pot ontology of bottom by waste-heat recovery device.
Preferably, several heat exchanger tubes are installed, each heat exchanger tube is fixed through burning cavity in the burning cavity
Setting, by the way that several heat exchanger tubes through burning cavity are arranged, for increasing the contact area of burning cavity and water, to increase
The heat exchange area of burning cavity improves the evaporation efficiency of water.
Preferably, the burning cavity bottom is equipped with detection pipe, and the detection pipe is connected to burning cavity bottom, combustion chamber
The detection pipe of body bottom setting connection, can be used for detecting whether burning cavity seeps water, and be conducive to repairing in time for burning cavity
It mends.
Preferably, the bottom of the bottom pot ontology is equipped with drainpipe, and the drainpipe is connected to bottom pot ontology, bottom pot ontology
With burning cavity during prolonged use, it is easy to produce scale, scale can reduce the heat transference efficiency of burning cavity, this
Device is needed before snaking per progress snaking processing after a period of use, is required by the intrinsic residual water discharge of bottom pot
Completely, it by the way that drainpipe is arranged in the bottom of bottom pot ontology, discharges the bottom intrinsic water of pot completely, carries out bottom pot to facilitate
Ontology and the operation of the snaking of burning cavity.
Compared with the prior art, the advantages of the present invention are as follows：The heating wine retort bottom pot system of waste heat, bottom can be recycled in the present invention
A certain amount of water is added in pot ontology, keeps heat exchanger submerged in water, is heated using burner heat exchanging device, heat exchanger produces
Raw heat is fully absorbed by the bottom intrinsic water of pot, and burn in the heat exchanger high-temperature tail gas of generation of fuel enters waste heat
Recyclable device heats the water in waste-heat recovery device, and waste-heat recovery device is connected to bottom pot ontology, and the water after heating can
For supplementing evaporation water in the pot ontology of bottom, to greatly improve the thermal efficiency of the present apparatus, waste-heat recovery device is also connect with transition
Head circulation connection, transit joint are returned for connecting heat exchanger exit end and combustor arrival end, water flow along transit joint and waste heat
Receiving apparatus circulates, and can play the role of cooling protection connectivity port but also be used to cool down by the high temperature that connectivity port generates
The heating of water has reached the function of the recycling of waste heat, and the more conventional distillation rice steamer bottom pot of the present apparatus, heat loss is small, the damage of energy
It consumes low, the service life of the connectivity port of heat exchanger and combustor can be extended, so that brewing cost be greatly saved.
The beneficial effect of the application other embodiments is：
1. under the action of water pressure, pot intrinsic water in bottom enters in liquid level tube, bottom pot ontology and liquid level tube is made to keep identical
Liquid level, by observing the liquid level of liquid level tube it can be learnt that the intrinsic water of bottom pot, consequently facilitating in time to bottom pot ontology
It is inside automatically replenished evaporation water, is avoided in use since water is very few, heat exchanger is not totally submerged caused by Yu Shuizhong
Thermal loss.
2. liquid level sensor is to export the form that the high-degree of conversion of liquid level is electric signal, liquid level sensor can be used for
Water surface elevation in detection liquid level tube detects the intrinsic liquid level of bottom pot in turn, and liquid level sensor includes along liquid level tube
The vertically arranged top photoelectric probe of wall, middle part photoelectric probe and lower part photoelectric probe, when liquid level decline, middle part light in liquid level tube
When electric probe is not contacted with liquid level, middle part photoelectric probe receives inductive signal, and is converted into electric signal by liquid level sensor and passes
It is handed to control device, the electromagnetic valve of control device control waste-heat recovery device automatically opens, the intrinsic evaporation of supplement bottom pot
With water until when top photoelectric probe and liquid level contact, top photoelectric probe receives inductive signal, and is turned by liquid level sensor
It turns to electric signal and is transferred to control device, control device control electromagnetic valve is automatically closed, to realize by waste-heat recovery device
Be automatically replenished the process of evaporation water from the pot ontology of trend bottom, when in waste-heat recovery device without add in time cooling water and
When cannot continue to supplement the bottom intrinsic evaporation water of pot, the present apparatus in use, held with water by the bottom intrinsic evaporation of pot
Continuous to reduce, when lower part, photoelectric probe is not contacted with liquid level, lower part photoelectric probe receives inductive signal, and passes through liquid level sensor
It is converted to electric signal and is transferred to control device, the electromagnetic valve on combustor tracheae is controlled by control device and is automatically closed, is stopped
Only combustor heat exchanging device continues to heat, to avoid since evaporation water is very few in the pot ontology of bottom, the heat that heat exchanger generates
It cannot be taken away in time, bottom pot ontology is caused to be damaged by high temperature.
3. pumping plant circulates in waste-heat recovery device and transit joint for water and provides power, recirculated cooling water
The high temperature heat at heat exchanger entrance end and combustor outlet end position can be taken away in time, had and protected connectivity port not by high temperature
The effect of damage, and cooling water also is heated using high temperature heat, and then realize the secondary use of high temperature heat, burning
Machine outlet end and heat exchanger entrance end are detachably connected with transit joint respectively, can facilitate transit joint and combustor outlet end and
The installation at heat exchanger entrance end and the replacement of transit joint.
4. air and fuel are pressed proper proportion mix and convert by pre-mixing apparatus so that it is abundant in burning cavity by combustor
Burning, the high-temp waste gas generated after burning can store cavity by exhaust gas and store discharge in time, and exhaust gas in burning cavity is avoided to arrange
Put the full combustion for influencing fuel not in time.
5. high-temp waste gas enters in exhaust pipe along exhaust gas storage cavity, exhaust pipe is installed in sink, can be used for sink
Interior water is heated, and is realized to the heat recovery in high-temp waste gas, the water after heating is being added in the pot ontology of bottom, realized
The secondary use of waste-gas heat, to improve the heat utilization ratio of boiler.
6. the bottom of sink is connected to bottom pot ontology using pipeline, waste-heat recovery device is installed on the top of bottom pot ontology,
When requiring supplementation with the bottom intrinsic evaporation water of pot, electromagnetic valve is opened, is installed by waste-heat recovery device and bottom pot ontology
The hydraulic pressure effect that the difference in height of position generates automatically flows into water in the pot ontology of bottom by waste-heat recovery device.
7. by the way that several heat exchanger tubes through burning cavity are arranged, for increasing the contact area of burning cavity and water, from
And increase the heat exchange area of burning cavity, improve the evaporation efficiency of water.
8. the detection pipe of burning cavity bottom setting connection, can be used for detecting whether burning cavity seeps water, is conducive to
The timely repairing of burning cavity.
9. bottom pot ontology and burning cavity are easy to produce scale, scale can reduce burning during prolonged use
The heat transference efficiency of cavity, the present apparatus are needed before snaking per progress snaking processing after a period of use, is required by bottom pot
Intrinsic residual water discharge is clean, by the way that drainpipe is arranged in the bottom of bottom pot ontology, arranges the bottom intrinsic water of pot completely
It puts, to facilitate the snaking operation for carrying out bottom pot ontology and burning cavity.
Detailed description of the invention
Fig. 1 is each equipment connection schematic diagram of heating wine retort bottom pot system of the recyclable waste heat of the present invention；
Fig. 2 is the structural schematic diagram of the heating wine retort bottom pot system of the recyclable waste heat of the present invention；
Fig. 3 is the structural schematic diagram of the heat exchanger of the heating wine retort bottom pot system of the recyclable waste heat of the present invention；
Fig. 4 is the structural schematic diagram of the waste-heat recovery device of the heating wine retort bottom pot system of the recyclable waste heat of the present invention；
Fig. 5 is that the transit joint of the heating wine retort bottom pot system of the recyclable waste heat of the present invention goes out with combustor arrival end and heat exchanger
The decomposition texture schematic diagram at mouth end；
Fig. 6 is the structural schematic diagram of the transit joint of the heating wine retort bottom pot system of the recyclable waste heat of the present invention；
Fig. 7 is the structural representation of the section in the orientation transit joint A-A of the heating wine retort bottom pot system of the recyclable waste heat of the present invention
Figure.
Appended drawing reference
1- combustor, the bottom 2- pot ontology, 3- heat exchanger, 31- exhaust gas store cavity, 32- burning cavity, 33- heat exchanger tube, 4- waste heat
Recyclable device, 41- flue gas leading, 42- sink, 5- upper cover, 6- liquid level tube, the top 61- photoelectric probe, the middle part 62- photoelectricity are visited
Head, the bottom 63- photoelectric probe, 7- control device, 8- drainpipe, 9- detection pipe, 10- steam lattice, 11- adapter tube, and 12- transition connects
Head, 13- combustor outlet end, 14- heat exchanger entrance end, 15- pipeline.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to the accompanying drawings and embodiments, right
The present invention is further elaborated.It should be appreciated that described herein, specific examples are only used to explain the present invention, not
For limiting the present invention.
Embodiment 1
The wine rice steamer of waste heat can be recycled in the present embodiment as shown in attached drawing 1, attached drawing 2, attached drawing 3, attached drawing 4, attached drawing 5, attached drawing 6 and attached drawing 7
Bottom pot heating system includes combustor 1, bottom pot ontology 2, heat exchanger 3, and exhaust gas stores cavity 31, burning cavity 32, heat exchanger tube 33,
Waste-heat recovery device 4, flue gas leading 41, sink 42, upper cover 5, liquid level tube 6, top photoelectric probe 61, middle part photoelectric probe
62, bottom photoelectric probe 63, control device 7, drainpipe 8, detection pipe 9, steaming lattice 10, adapter tube 11, transit joint 12, combustor goes out
The water of about 0.8T is added in mouth end 13, heat exchanger entrance end 14, pipeline 15 into bottom pot ontology 2 first, will steam lattice 10 and is placed in bottom
Pot ontology 2 on, then by upper cover 5 be buckled in bottom pot ontology 2 on, by the fermenting-ripening grain unstrained spirits distilled be placed in steaming lattice 10
On, conventional distillation rice steamer bottom pot is directly heated using 1 pair of bottom of combustor, 2 bottom of pot ontology, and 0.8T water is using 150,000 kilocalories/small
When combustor need to heat 20 minutes, so that water temperature is reached 100 DEG C of fluidized states, whole process takes around consumption 50,000
Kilocalorie energy, and in evaporation process, it needs to supplement evaporation water, water is used in evaporation according to the water variation in the pot ontology 2 of bottom
Be added bottom pot ontology 2 before also require heat to certain temperature, with reach be added bottom pot ontology 2 after fast boiling evaporate mesh
, the present apparatus is totally submerged in water using heat exchanger 3, it is heated using 1 heat exchanging device 3 of combustor, what heat exchanger 3 generated
Heat directly by bottom pot ontology 2 in water absorb after be used for white liquor distilling, heat loss is small, 0.8T water heating only need 10 minutes i.e.
Can ebuillition of heated, thus greatly reduce energy consumption, and the high-temp waste gas generated in 3 heating process of heat exchanger enters waste heat recycling
Device 4, and the water in waste-heat recovery device 4 is heated, waste-heat recovery device 4 is connected to bottom pot ontology 2, the water after heating
The evaporation water that can be directly used in the pot ontology 2 of supplement bottom realizes energy to save the capacity loss of heating evaporation water
Secondary use improves the thermal efficiency of boiler, and waste-heat recovery device 4 is also connected to the circulation of transit joint 12, and transit joint 12 is used for
Heat exchanger exit end 14 and combustor arrival end 13 are connected, water flow is circulated along transit joint 12 and waste-heat recovery device 4, both
Can play the role of cooling protection connectivity port again can be used for the high temperature heat of connectivity port the heating of cooling water, reach remaining
The function of the recycling of heat, the more conventional distillation rice steamer bottom pot of the present apparatus, heat loss is small, and low energy consumption, can extend heat exchanger 3 and combustion
The service life of the connectivity port of burning machine 1 can substantially reduce brewing cost.
Under the action of water pressure, the water in bottom pot ontology 2 enters in liquid level tube 6, and bottom pot ontology 2 and liquid level tube 6 is made to keep phase
Same liquid level, liquid level tube 6 are made of transparent material, by observing the liquid level of liquid level tube 6 it can be learnt that in the pot ontology 2 of bottom
Water, consequently facilitating in time to bottom pot ontology 2 in be automatically replenished evaporation water, avoid in use due to water mistake
Few, heat exchanger 3 is not totally submerged thermal loss caused by Yu Shuizhong.
Liquid level sensor is to export the high-degree of conversion of liquid level as electronic signals, is equipped in control device 7
The programmable chip of PLC, can receive electric signal and control electromagnetic valve movement, and liquid level sensor selection photoelectric liquid level sensor is
Using light in the novel touch point liquid-level measuring-controlling apparatus that reflected refraction principle occurs for two kinds of extended medias and develops, it has
Have that structure is simple, positioning accuracy is high;There is no mechanical part, is not required to debug;High sensitivity and corrosion-resistant;Little power consumption;It is small in size etc.
Plurality of advantages, due to liquid level output only other characteristics that liquid level is related, with medium whether are contacted with photoelectric probe, as temperature,
The parameters such as pressure, density, electricity are unrelated, so photoelectric liquid level sensor detection is accurate, repeatable accuracy is high;Fast response time, liquid level
Control is very accurate, and is not required to adjustment, so that it may it is mounted directly use, photoelectric liquid level sensor probe size is relatively small and exquisite,
It is mountable to be suitble to use in special tank body or container in small space, in addition it can install multiple light on a measurement body
Electric probe is made multiple spot liquid level sensor, becomes control device, and liquid level sensor includes along the top of 6 inner wall vertical position of liquid level tube installation
Photoelectric probe 61, middle part photoelectric probe 62 and lower part photoelectric probe 63, when liquid level decline, middle part photoelectric probe 62 in liquid level tube 6
When not contacting with liquid level, middle part photoelectric probe 62 receives inductive signal, and is converted into electric signal by liquid level sensor and is transferred to
Control device 7, the electromagnetic valve that control device 7 controls waste-heat recovery device 4 automatically open, the evaporation in the pot ontology 2 of supplement bottom
With water until when top photoelectric probe 61 and liquid level contact, top photoelectric probe 61 receives inductive signal, and passes through level sensing
Device is converted into electric signal and is transferred to control device 7, and the electromagnetic valve that control device 7 controls waste-heat recovery device 4 is automatically closed, from
And realize the process for being automatically replenished evaporation water from the pot ontology 2 of trend bottom by waste-heat recovery device 4, when waste-heat recovery device 7
It is interior without in time add cooling water and cannot continue supplement bottom pot intrinsic evaporation water when, the present apparatus is in use process
In, the evaporation in the pot ontology 2 of bottom is persistently reduced with water, when lower part photoelectric probe 63 is not contacted with liquid level, lower part photoelectric probe
63 receive inductive signal, and are converted to electric signal by liquid level sensor and are transferred to control device 7, are controlled by control device 7
Electromagnetic valve on 1 tracheae of combustor is automatically closed, and stops 1 heat exchanging device 3 of combustor and continues to heat, to avoid due to bottom pot
Evaporation is very few with water in ontology 2, and the heat that heat exchanger 3 generates cannot be taken away in time, and bottom pot ontology 2 is caused to be damaged by high temperature,
When in lower part, photoelectric probe 63 and liquid level are contacted, lower part photoelectric probe 63 receives inductive signal, and is converted by liquid level sensor
It is transferred to control device 7 for electric signal, the electromagnetic valve on 1 tracheae of combustor is controlled by control device 7 and is automatically opened.
Pumping plant provides power along the flowing of pipeline 15 in waste-heat recovery device 4 and transit joint 12 for water, recycles cold
But water can take away the high temperature heat at heat exchanger entrance end 14 and 13 position of combustor outlet end in time, have protection connectivity port
The effect not damaged by high temperature, and cooling water also is heated using high temperature heat, and then realize the secondary benefit of high temperature heat
With combustor outlet end 13 and heat exchanger entrance end 14 are detachably connected with transit joint 12 respectively, can facilitate transit joint 12
The replacement of installation and transit joint 12 with combustor outlet end 13 and heat exchanger entrance end 14.
Air and fuel are pressed proper proportion mix and convert by pre-mixing apparatus so that it is abundant in burning cavity 32 by combustor 1
Burning, the high-temp waste gas generated after burning can store the storage discharge in time of cavity 31 by exhaust gas, avoid giving up in burning cavity 32
Gas discharge causes insecurity factor not in time, and exhaust gas storage cavity 31 has guiding role, and bootable exhaust gas is along certain side
To outlet, be conducive to improve manual operation environment.
High-temp waste gas enters along flue gas leading along exhaust gas storage cavity 31, and flue gas leading 41 is installed in sink 42, can be used for pair
Water in sink 42 is heated, and the flue gas leading 41 in sink 42 is several interconnected annular coil pipes, annular coil pipe submergence
In water, exhaust gas can be achieved sufficiently to recycle the heat in high-temp waste gas along coil pipe flowing, and the water in sink 42 is by absorbing tail
The heat of gas can be heated to 90 DEG C, can be directly used for supplement evaporation water, the secondary use of waste-gas heat is realized, to mention
The high heat utilization ratio of boiler.
The bottom of sink 42 is connected to bottom pot ontology 2 using pipeline, and waste-heat recovery device 4 is installed on the upper of bottom pot ontology 2
Side opens electromagnetic valve when requiring supplementation with the evaporation water in the pot ontology 2 of bottom, passes through waste-heat recovery device 4 and bottom pot ontology
The hydraulic pressure effect that the difference in height of 2 installation sites generates, water are automatically flowed into the pot ontology 2 of bottom by waste-heat recovery device 4 along adapter tube 11.
Heat exchanger tube 33 runs through burning cavity 32, and the upper and lower ends of heat exchanger tube 33 and the above and below of burning cavity 32 are welded and connected
It connects, water is avoided to enter in burning cavity 32 along the connection gap of heat exchanger tube 33 and burning cavity 32, water can enter in heat exchanger tube 33
To increase the contact area of burning cavity 32 Yu water, and then increase the heat exchange area of burning cavity 32, improves the evaporation effect of water
Rate.
Whether the detection pipe 9 of 32 bottom of burning cavity setting connection, can be there are flowing out by detection pipe 9, judge combustion chamber
Whether body 32 seeps water, and is conducive to the timely repairing of burning cavity 32.
Bottom pot ontology 2 and burning cavity 32 are easy to produce scale, scale can reduce burning during prolonged use
The heat transference efficiency of cavity 32, the present apparatus need before snaking the bottom of by per progress snaking processing after a period of use, is required
Residual water discharge in pot ontology 2 is clean, by the way that drainpipe 8 is arranged in the bottom of bottom pot ontology 2, makes the water in the pot ontology 2 of bottom
Discharge completely, to facilitate the snaking operation for carrying out bottom pot ontology 2 and burning cavity 32.
Above embodiments are only to illustrate the present invention and not limit the technical scheme described by the invention, although this explanation
The present invention has been described in detail referring to above-mentioned each embodiment for book, but the present invention is not limited to above-mentioned specific implementation
Mode, therefore any couple of present invention modifies or equivalent replacement；And the technical side of all spirit and scope for not departing from invention
Case and its improvement, are intended to be within the scope of the claims of the invention.
Claims (10)
1. the heating wine retort bottom pot system of recyclable waste heat, including upper cover and bottom pot ontology, it is characterised in that：It further include peace
Loaded on the intrinsic heat exchanger of bottom pot, the heat exchanger is connected to combustor and waste-heat recovery device respectively, the waste heat recycling
Device is also connected to bottom pot ontology, and the waste-heat recovery device is also connected to transit joint circulation；The combustor is for exchanging
Hot device heating, the heat exchanger are used to heat the intrinsic evaporation water of bottom pot, the waste heat recycling dress by thermaltransmission mode
It sets and is recycled for waste-gas heat, the transit joint is for connecting heat exchanger entrance end and combustor outlet end.
2. the heating wine retort bottom pot system of recyclable waste heat according to claim 1, it is characterised in that：It further include having liquid level
Pipe, the liquid level tube are connected to bottom pot ontology.
3. the heating wine retort bottom pot system of recyclable waste heat according to claim 2, it is characterised in that：In the liquid level tube
Liquid level sensor is installed, the liquid level sensor includes top photoelectric probe, middle part photoelectric probe and lower part photoelectricity on wall
Probe, state liquid level sensor by control device respectively with the electromagnetism on the electromagnetic valve of waste-heat recovery device and combustor tracheae
Valve electrical connection.
4. the heating wine retort bottom pot system with the recyclable waste heat stated according to claim 3, it is characterised in that：The transit joint is
Cavity structure, the heat exchanger entrance end and combustor outlet end are detachably connected with transit joint respectively, the transit joint
Pumping plant is installed on the pipeline being connected by circulation with waste-heat recovery device.
5. the heating wine retort bottom pot system of recyclable waste heat according to claim 1 to 4, it is characterised in that：It is described to change
Hot device includes burning cavity and exhaust gas storage cavity, and the burning cavity is connected to combustor and exhaust gas storage cavity respectively.
6. the heating wine retort bottom pot system of recyclable waste heat according to claim 5, it is characterised in that：The waste heat recycling
Device includes sink and the flue gas leading that is installed in sink, and the flue gas leading is stored cavity with exhaust gas and is connected to.
7. the heating wine retort bottom pot system of recyclable waste heat according to claim 6, it is characterised in that：The waste heat recycling
Device is installed on the top of bottom pot ontology, and the bottom of the sink is connected to bottom pot ontology using adapter tube.
8. the heating wine retort bottom pot system of recyclable waste heat according to claim 7, it is characterised in that：The burning cavity
Several heat exchanger tubes are inside installed, each heat exchanger tube is fixedly installed through burning cavity.
9. the heating wine retort bottom pot system of recyclable waste heat according to claim 8, it is characterised in that：The burning cavity
Bottom is equipped with detection pipe, and the detection pipe is connected to burning cavity bottom.
10. the heating wine retort bottom pot system of recyclable waste heat according to claim 1, it is characterised in that：The bottom pot is originally
The bottom of body is equipped with drainpipe, and the drainpipe is connected to bottom pot ontology.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810969550.2A CN108841557A (en) | 2018-08-23 | 2018-08-23 | The heating wine retort bottom pot system of recyclable waste heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810969550.2A CN108841557A (en) | 2018-08-23 | 2018-08-23 | The heating wine retort bottom pot system of recyclable waste heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108841557A true CN108841557A (en) | 2018-11-20 |
Family
ID=64188261
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810969550.2A Pending CN108841557A (en) | 2018-08-23 | 2018-08-23 | The heating wine retort bottom pot system of recyclable waste heat |
Country Status (1)
| Country | Link |
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| CN (1) | CN108841557A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0246376A1 (en) * | 1986-05-23 | 1987-11-25 | Glen Sundquist | Water heater and distiller apparatus |
| CN1683510A (en) * | 2005-02-07 | 2005-10-19 | 四川绵竹剑南春酒厂有限公司 | Wine rice steamer bottom pot |
| CN1683509A (en) * | 2005-02-06 | 2005-10-19 | 四川绵竹剑南春酒厂有限公司 | Distilling device for producing white spirit |
| CN204079945U (en) * | 2014-08-18 | 2015-01-07 | 温州鸿马科技有限公司 | A kind of white liquor distilling equipment of water coolant recycling |
| CN205170811U (en) * | 2015-12-05 | 2016-04-20 | 四川宜宾岷江机械制造有限责任公司 | Pot at bottom of energy -conserving direct combustion formula of making wine gas |
| CN206298571U (en) * | 2016-12-16 | 2017-07-04 | 哈尔滨工大金涛科技股份有限公司 | A kind of alcoholic system waste heat retracting device |
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2018
- 2018-08-23 CN CN201810969550.2A patent/CN108841557A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0246376A1 (en) * | 1986-05-23 | 1987-11-25 | Glen Sundquist | Water heater and distiller apparatus |
| CN1683509A (en) * | 2005-02-06 | 2005-10-19 | 四川绵竹剑南春酒厂有限公司 | Distilling device for producing white spirit |
| CN1683510A (en) * | 2005-02-07 | 2005-10-19 | 四川绵竹剑南春酒厂有限公司 | Wine rice steamer bottom pot |
| CN204079945U (en) * | 2014-08-18 | 2015-01-07 | 温州鸿马科技有限公司 | A kind of white liquor distilling equipment of water coolant recycling |
| CN205170811U (en) * | 2015-12-05 | 2016-04-20 | 四川宜宾岷江机械制造有限责任公司 | Pot at bottom of energy -conserving direct combustion formula of making wine gas |
| CN206298571U (en) * | 2016-12-16 | 2017-07-04 | 哈尔滨工大金涛科技股份有限公司 | A kind of alcoholic system waste heat retracting device |
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Application publication date: 20181120 |
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