CN110106292A - A kind of continuous boiling pan draining system of brown sugar - Google Patents
A kind of continuous boiling pan draining system of brown sugar Download PDFInfo
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- CN110106292A CN110106292A CN201910463625.4A CN201910463625A CN110106292A CN 110106292 A CN110106292 A CN 110106292A CN 201910463625 A CN201910463625 A CN 201910463625A CN 110106292 A CN110106292 A CN 110106292A
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- separation cylinder
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- 238000009835 boiling Methods 0.000 title claims abstract description 137
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 253
- 230000000694 effects Effects 0.000 claims abstract description 92
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 230000002459 sustained effect Effects 0.000 claims abstract description 4
- 238000000926 separation method Methods 0.000 claims description 58
- 210000000038 chest Anatomy 0.000 claims description 39
- 238000001816 cooling Methods 0.000 claims description 29
- 230000006837 decompression Effects 0.000 claims description 26
- 238000003756 stirring Methods 0.000 claims description 17
- 239000000523 sample Substances 0.000 claims description 15
- 229910000831 Steel Inorganic materials 0.000 claims description 9
- 239000010959 steel Substances 0.000 claims description 9
- 238000007789 sealing Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 4
- 235000014121 butter Nutrition 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 235000014171 carbonated beverage Nutrition 0.000 description 5
- 238000005299 abrasion Methods 0.000 description 4
- 239000008234 soft water Substances 0.000 description 4
- 238000004134 energy conservation Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000006188 syrup Substances 0.000 description 3
- 235000020357 syrup Nutrition 0.000 description 3
- 238000010411 cooking Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000009923 sugaring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B25/00—Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
- Commercial Cooking Devices (AREA)
Abstract
The present invention provides a kind of continuous boiling pan draining system of brown sugar, including pedestal, upper water box, intermediate water tank, lower header, water pump, first steam-water separator, second steam-water separator, boiling pan, heating plant and water circle device, intermediate water tank and two effect boiling pans are located at sustained height, first venthole is connect by pipeline with the air intake of the first steam-water separator, the water outlet of first steam-water separator is connected by the water inlet of pipeline and intermediate water tank, the water outlet of intermediate water tank is connected by the water inlet of pipeline and lower header, water pipe is equipped between intermediate water tank and heating plant, water pump is used to the water in lower header being pumped into upper water box, second venthole is connect by pipeline with the air intake of the second steam-water separator, the water outlet of second steam-water separator connects the water inlet of lower header by pipeline.The utilization rate that can solve hot water during brown sugar cooks is low, and hot water is caused to waste serious technical problem.
Description
Technical field
The present invention relates to sugar mill technical field more particularly to a kind of continuous boiling pan draining systems of brown sugar.
Background technique
Currently, will use continuous boiling pan, the technique that continuous boiling pan is refined sugar during brown sugar cooks are as follows: sugar
Slurry is introduced into an effect boiling pan and cooks a period of time, is put into two effect boiling pans after reaching corresponding brix, two effect boiling pans boil
Next process is entered back into after corresponding brix, this process is a continuous process, that is to say, that syrup passes in and out boiling pan
It is all continuous.The heat supply of brown sugar boiling pan at present is the raw vapour of boiler after directlying adopt cooling decompression, after cooling decompression
Raw steam pressure is 0.6MP, and temperature is 200 DEG C.There are three steam chests for the boiling pan of one effect, and there are two steam chests for two effect boiling pans, this is several
A steam chest be it is independent, the life vapour of boiler is exactly by this few steam chest.The cooking of syrup is exactly the heat transmitting by raw vapour
Syrup is cooked, in this process, raw vapour has a process for cooling, and it is solidifying will to generate during this cooling vapour
Water, and the life vapour of boiler belongs to saturated vapor, and the amount that vapor condensed water generates is more, so draining system is just extremely important, dredges
The effect quality of water, directly affects the usage amount of raw vapour during sugaring.
The vapor condensed water of boiling pan is by being generally exhausted directly in atmosphere, none vapor condensed water after hydrophobic in sugar refinery
The system of collection, therefore a set of vapor condensed water cyclic utilization system need to be designed.
Summary of the invention
The technical problems to be solved by the present invention are: a kind of continuous boiling pan draining system of brown sugar is provided, to solve red
The utilization rate of hot water is low during candy system, and hot water is caused to waste serious technical problem.
In order to solve the above technical problems, the technical scheme is that a kind of continuous boiling pan draining system of brown sugar, including
Pedestal, upper water box, boiling pan, heating plant and water circle device, the upper water box are fixedly installed at the top of the pedestal；Institute
Stating boiling pan includes an effect boiling pan and two effect boiling pans, and the effect boiling pan is installed on the pedestal and is located on described
Below water tank, the effect boiling pan is equipped with feed inlet, and effect boiling pan bottom is equipped with the first steam chest, first steam chest
Equipped with the first air intake and the first venthole, the two effects boiling pan is installed on the pedestal and is located at the effect boiling pan
Lower section, two effect boiling pan bottom are equipped with the second steam chest, and second steam chest is equipped with the second air intake and the second venthole；Institute
Stating heating plant and connecting first air intake is the first steam chest steam supply；The water circle device include intermediate water tank, under
Water tank, water pump, the first steam-water separator and the second steam-water separator, the intermediate water tank be installed on the pedestal and with institute
It states two effect boiling pans and is located at sustained height, the lower header is set to below the two effects boiling pan, and first venthole passes through
Pipeline is connect with the air intake of first steam-water separator, the water outlet of first steam-water separator by pipeline with it is described
The water inlet of intermediate water tank connects, and the water outlet of the intermediate water tank is connect by pipeline with the water inlet of the lower header, institute
It states and is equipped with water-supply-pipe between intermediate water tank and the heating plant, the water outlet of the lower header connects the upper water by pipeline
Case, the water pump are installed between the lower header and the upper water box for the water in the lower header to be pumped into the upper water
Case, second venthole are connect by pipeline with the air intake of second steam-water separator, second steam-water separator
Water outlet the water inlet of the lower header is connected by pipeline.
As an improvement mode, first steam-water separator include the first steam-water separation cylinder, first carbonated drink
Venthole is equipped at the top of cylinder, the first steam-water separation cylinder side is equipped with the air intake for being connected to first steam chest,
The first steam-water separation cylinder bottom is taper and is equipped with water outlet；Second steam-water separator includes the second steam-water separation
Cylinder, the second steam-water separation cylinder top are equipped with venthole, and the second steam-water separation cylinder side is equipped with for being connected to second vapour
The air intake of room, the second steam-water separation cylinder bottom are taper and are equipped with water outlet.
As an improvement mode, the height of the first steam-water separation cylinder and the second steam-water separation cylinder is
0.8~1.2 meter, equal 0.24~0.26 meter of internal diameter of the first steam-water separation cylinder and the second steam-water separation cylinder.
As an improvement mode, the air intake of the first steam-water separation cylinder side is apart from first steam-water separation
The distance of cylinder top venthole is greater than 0.5 meter；The air intake of the second steam-water separation cylinder side is apart from second carbonated drink point
It is greater than 0.5 meter with a distance from venthole at the top of cylinder.
As an improvement mode, further include agitating device, the agitating device includes agitating shaft, stirring motor, axis
Seat and stirring blade are held, the agitating shaft extends transversely through the effect boiling pan, the both ends of the agitating shaft and an effect
Sealing device is respectively equipped between boiling pan, the both ends of the agitating shaft are respectively equipped with an institute outside the effect boiling pan
Bearing block is stated, two bearing blocks are individually fixed on the effect boiling pan, and the agitating shaft and stirring motor transmission connect
It connects, the stirring blade is set in the effect boiling pan and is installed on the agitating shaft.
As an improvement mode, further include temperature measuring equipment, it is described one effect boiling pan left side be equipped with feed inlet, institute
The lower right side for stating an effect boiling pan is equipped with discharge port, and multiple first vapour are equipped between the feed inlet and the discharge port
Room, the temperature measuring equipment include temperature probe and display, and the effect boiling pan is interior in the outer of each first steam chest
The temperature probe is respectively equipped on side wall, each temperature probe connects the display, the survey by thermometric line
Warm line outer cover is equipped with steel pipe, and the steel pipe is fixed on the inner sidewall of the effect boiling pan.
As an improvement mode, the heating plant includes boiler and cooling decompression station, and first air intake is logical
Piping connects cooling decompression station, and the cooling decompression station connects boiler by pipeline, and the steam that the boiler generates passes through institute
It is passed through first steam chest after stating cooling decompression station, the intermediate water tank connects cooling decompression station by water-supply-pipe and supplies water for it.
As an improvement mode, it is described two effect boiling pan be equipped with agitating device and temperature measuring equipment.
Acquired technical effect by adopting the above technical scheme are as follows:
First steam-water separator carries out vapour to the steam being discharged in an effect boiling pan, water separates and will condense resulting hot water
It is delivered to the cooling decompression station in intermediate water tank for heating plant and hot water supply is provided, the cooling decompression standing-meeting of heating plant uses
The vapor condensed water of endless effect boiling pan, intermediate water tank make exhaustless vapor condensed water be collected into lower header by an overflow passage handle
It is interior.Second steam-water separator carries out vapour to the steam being discharged in two effect boiling pans, water separates and will condense resulting delivery
To lower header, the cooling decompression station with heating plant collects exhaustless vapor condensed water together.Pass through the heat of pump handle lower header
Water is evacuated to upper water box, uses as production technology hot water, in entire production process, due to that can often need to using to hot water,
Such as cleaning boiling pan, overrich needs to add hot water etc. when boiling sugar, and by this whole improvement, hot water, which may be implemented, to be made
It is self-sufficient, and the environment on periphery is not influenced, therefore the continuous boiling pan draining system energy conservation and environmental protection of brown sugar of the application,
The waste for reducing water resource, effectively reduces production cost.
Since the air intake of the first steam-water separation cylinder side is apart from the first steam-water separation cylinder top venthole
Distance is greater than 0.5 meter；The air intake of second steam-water separation cylinder side venthole at the top of the second steam-water separation cylinder
Distance be greater than 0.5 meter.When steam and vapor condensed water together toward outlet when, elder generation is in the first steam-water separation cylinder side wall or the second vapour
Buffering in water cylinder side wall, steam is arranged upwards again, due to vapor condensed water self gravity, can only arrange general 0.5 meter upwards
Left and right will fall, and distance of the air intake distance of two steam-water separation cylinder sides respectively at the top of it, which is greater than 0.5 meter and can guarantee, steams
Vapour sufficiently condenses in steam-water separation cylinder.
Due to further including agitating device, the agitating device includes agitating shaft, stirring motor, bearing block and paddle
Piece, the agitating shaft extend transversely through the effect boiling pan, between the both ends of the agitating shaft and the effect boiling pan respectively
Equipped with sealing device, the both ends of the agitating shaft are imitated in described one is respectively equipped with the bearing block outside boiling pan, and two
Bearing block is individually fixed on the effect boiling pan, and the agitating shaft and the stirring motor are sequentially connected, the paddle
Piece is set in the effect boiling pan and is installed on the agitating shaft.The brown sugar boiling pan of the application is bearing block and boiling pan
Tank body separates, and the mode that encryption seal ring can be used in the position that agitating shaft is connect with tank body is sealed.The application's
Brown sugar boiling pan bearing fill butter lubrication when be not in the case where butter enters boiling pan, thoroughly solve butter into
The problem of entering boiling pan, and this design installation is simple and can observe the abrasion condition of bearing block constantly, it can be according to axis
The abrasion condition for holding seat periodically fills butter, also greatly reduces to the usage amount of butter, to reduce costs.
Due to further including temperature measuring equipment, the left side of the effect boiling pan is equipped with feed inlet, the effect boiling pan
Lower right side is equipped with discharge port, and multiple first steam chests, the thermometric dress are equipped between the feed inlet and the discharge port
It sets including temperature probe and display, is respectively equipped in the effect boiling pan on the lateral wall of each first steam chest
One temperature probe, each temperature probe connect the display by thermometric line, and the thermometric line outer cover is equipped with
Steel pipe, the steel pipe are fixed on the inner sidewall of the effect boiling pan.The medium position of each steam chest is separately installed with thermometric
Probe, can know constantly tank interior material is how many in each section of actual temperature by temperature measuring equipment, so as to reasonable
The raw vapour of control boiler pressure, temperature measuring equipment can also be connect with robot control system(RCS), according to the temperature of each temperature control point to each
The life steam pressure of steam chest carries out automatically controlling, as long as setting required temperature of charge, so that it may automatically control the pressure of raw vapour
Power realizes automation control, reduces manually, and quality is more stable.
Detailed description of the invention
Present invention will be further explained below with reference to the attached drawings and examples.
Fig. 1 is the overall construction drawing of the continuous boiling pan draining system of brown sugar of the invention；
Fig. 2 is the structure chart of steam-water separator of the invention；
Fig. 3 is the structural schematic diagram of an effect boiling pan；
Fig. 4 be in Fig. 3 A-A to cross-sectional view；
1- pedestal, 101- feed inlet, 102- discharge port, 11- upper water box, 12- intermediate water tank, 13- lower header, 21- mono- are imitated
Boiling pan, the first steam chest of 211-, 22- bis- imitate boiling pan, the second steam chest of 221-, the first steam-water separator of 31-, the second carbonated drink of 32-
Separator, 311- steam-water separation cylinder, 312- air intake, 313- water outlet, 33- water pump, 41- agitating shaft, 42- stirring motor, 43-
Bearing block, 44- stirring blade, 51- temperature probe, 52- display, 53- steel pipe, 6- drain valve, 7- massecuite distributor.
Specific embodiment
As depicted in figs. 1 and 2, the continuous boiling pan draining system of a kind of brown sugar, including pedestal 1, upper water box 11, boiling pan,
Heating plant and water circle device, upper water box 11 are fixedly installed in 1 top of pedestal.Boiling pan includes an effect boiling pan 21 and two
Imitate boiling pan 22, an effect boiling pan 21 is installed on pedestal 1 and is located at the lower section of upper water box 11, and effect 21 bottom of boiling pan is equipped with the
One steam chest 211, the first steam chest 211 are equipped with the first air intake and the first venthole.Two effect boiling pans 22 be installed on pedestal 1 and
Positioned at 21 lower section of an effect boiling pan, two effect 22 bottoms of boiling pan are equipped with the second steam chest 221, and the second steam chest 221 is equipped with second into vapour
Mouth and the second venthole are equipped with conveying pipeline between two effect boiling pans 22 and an effect boiling pan 21, and two imitate the discharge port of boiling pans 22
Massecuite separator 7 is connected, massecuite separator 7 is used to be collected the brown sugar that cooking obtains.Heating plant includes boiler and drop
The setting height of warm pressure-reducing station, cooling decompression station should be lower than the setting height of two effect boiling pans 22, the high temperature and pressure that boiler generates
It is that an effect boiling pan 21 and two effects are boiled that steam, which connects the first air intake by pipeline after cooling decompression station carries out cooling decompression,
22 steam supply of sugar bowl.
Water circle device includes intermediate water tank 12, lower header 13, water pump 33, the first steam-water separator 31 and the second carbonated drink
Separator 32, intermediate water tank 12 are installed on pedestal 1 and are located at sustained height with two effect boiling pans 22, and lower header 13 is set to two effects
22 lower section of boiling pan, the first venthole are connect by being equipped with the pipeline of drain valve 6 with the air intake of the first steam-water separator 31, the
The water outlet of one steam-water separator 31 is connect by pipeline with the water inlet of intermediate water tank 12, and the water outlet of intermediate water tank 12 passes through
Pipeline is connect with the water inlet of lower header 13, and intermediate water tank 12 connects cooling decompression station by water-supply-pipe and supplies water for it.
The water outlet of lower header 13 connects upper water box 11 by pipeline, water pump 33 be installed on lower header 13 and upper water box 11 it
Between for the water pump 33 in lower header 13 to be entered upper water box 11, the second venthole, which passes through, is equipped with 6 pipeline of drain valve and the second carbonated drink
The air intake of separator 32 connects, and the water outlet of the second steam-water separator 32 connects the water inlet of lower header 13 by pipeline.
First steam-water separator 31 includes the first steam-water separation cylinder 311, is equipped with venthole at the top of the first steam-water separation cylinder 311
313,311 side of the first steam-water separation cylinder is equipped with the air intake for being connected to the first steam chest 211,311 bottom of the first steam-water separation cylinder
Portion is taper and is equipped with water outlet 312；Second steam-water separator 32 includes the second steam-water separation cylinder 311, the second steam-water separation cylinder
311 tops are equipped with venthole 312, and 311 side of the second steam-water separation cylinder is equipped with the air intake for being connected to the second steam chest 221, the
Two steam-water separation cylinders, 311 bottom is taper and is equipped with water outlet 313.
The height of first steam-water separation cylinder 311 and the second steam-water separation cylinder 311 is 0.8~1.2 meter, the first steam-water separation
Equal 0.24~0.26 meter of internal diameter of cylinder 311 and the second steam-water separation cylinder 311.The air intake of first steam-water separation cylinder, 311 side away from
It is greater than 0.5 meter with a distance from 311 top venthole of the first steam-water separation cylinder；The air intake of second steam-water separation cylinder, 311 side away from
It is greater than 0.5 meter with a distance from 311 top venthole of the second steam-water separation cylinder.When steam and vapor condensed water together toward outlet when, elder generation
It is buffered in the first steam-water separation cylinder 311 or the second steam-water separation cylinder 311, steam is arranged upwards again, due to vapor condensed water self gravity
The reason of, can only arrange general 0.5 meter or so upwards will fall, its respective top of the air intake distance of two steam-water separation cylinder sides
The distance in portion is greater than 0.5 meter of certifiable steam and sufficiently condenses in steam-water separation cylinder.
As shown in Figure 3 and Figure 4, the continuous boiling pan draining system of brown sugar further includes agitating device and temperature measuring equipment, stirring dress
It sets including agitating shaft 41, stirring motor 42, bearing block 43 and stirring blade 44, agitating shaft 41 extends transversely through an effect boiling pan
21, it is respectively equipped with sealing device between the both ends of agitating shaft 41 and an effect boiling pan 21, the both ends Yu Yixiao of agitating shaft 41 boils sugar
A bearing block 43 is respectively equipped with outside tank 21, two bearing blocks 43 are individually fixed on an effect boiling pan 21, agitating shaft 41 with
Stirring motor 42 is sequentially connected, and stirring blade 44 is set in an effect boiling pan 21 and is installed on agitating shaft 41.
The brown sugar boiling pan of the application separates bearing block and boiling pan tank body, the portion that agitating shaft 41 is connect with tank body
The mode that encryption seal ring can be used in position is sealed.The bearing of the brown sugar boiling pan of the application fill butter lubrication when not
It will appear the case where butter enters boiling pan, thoroughly solve the problems, such as that butter enters boiling pan, and this design is installed
Abrasion condition that is simple and can observing bearing block 43 constantly can periodically fill Huang according to the abrasion condition of bearing block 43
Oil is also greatly reduced the usage amount of butter, to reduce costs.
The left side of one effect boiling pan 21 is equipped with feed inlet 101, and the lower right side of an effect boiling pan 21 is equipped with discharge port
102, multiple first steam chests 211 are equipped between feed inlet 101 and discharge port 102, temperature measuring equipment includes temperature probe 51 and display
Device 52, in being respectively equipped with a temperature probe 51, each thermometric on the lateral wall of each the first steam chest 211 in an effect boiling pan 21
Probe 51 connects display 52 by thermometric line, and thermometric line outer cover is equipped with steel pipe 53, and steel pipe 53 is fixed on an effect boiling pan 21
Inner sidewall on.The medium position of each steam chest is separately installed with temperature probe 51, can be known constantly by temperature measuring equipment and be boiled
Sugar bowl tank interior material is how many in each section of actual temperature, so as to reasonably control the pressure of the raw vapour of boiler, may be used also
Temperature measuring equipment is connect with robot control system(RCS), is controlled automatically according to life steam pressure of the temperature of each temperature control point to each steam chest
System, as long as setting the temperature of charge for boiling sugar needs, so that it may which the pressure for automatically controlling raw vapour is realized automation control, reduced
It is artificial, and quality is more stable.Two effect boiling pans 22 can be equipped with and an effect mutually isostructural agitating device of boiling pan 21 and survey
Warm device.
The continuous boiling pan draining system course of work of the brown sugar of the application are as follows:
First steam-water separator 31 carries out vapour to the steam being discharged in an effect boiling pan 21, water separates and will condense resulting
Hot water supply is provided for cooling decompression station in delivery to intermediate water tank 12, cooling decompression station uses endless effect boiling pan 21
Vapor condensed water, intermediate water tank 12 is by overflow passage being collected into exhaustless vapor condensed water in lower header 13.Second vapour
Separator 32 is to the steam that is discharged carries out vapour, water separates in two effect boiling pans 22 and will condense resulting delivery to being lauched
Case 13 collects exhaustless vapor condensed water together with cooling decompression station.The hot water of lower header 13 is evacuated to upper water by water pump 33
Case 11 is used as production technology hot water, in entire production process, due to can often need to using to hot water, for example is cleaned
Boiling pan, overrich needs to add hot water etc. when boiling sugar, and by this whole improvement, the self-sufficiency that hot water uses may be implemented
It is self-sustaining, and the environment on periphery is not influenced, therefore the continuous boiling pan draining system energy conservation and environmental protection of brown sugar of the application, reduce water
The waste of resource, effectively reduces production cost.
The effect of first steam-water separator 31 is to collect vapor condensed water caused by an effect each steam chest of boiling pan 21, solidifying in vapour
When water passes through steam-water separator, steam is up arranged, and vapor condensed water follows tubes rows overflow to two effect boiling pans, 22 side down
Intermediate water tank 12 is collected hot water, and the effect of this intermediate water tank 12 is to provide hot water to cooling decompression station, and cooling subtracts
Pressure station meets the use at cooling decompression station it is desirable that soft water, just vapor condensed water belongs to soft water, and temperature has reached 100 DEG C
It is required that the usage amount of cooling decompression station soft water is 1 cube of each hour, and imitated caused by boiling pan 21 by measuring and calculating, one
Vapor condensed water amount has reached the amount of 2 cubes of each hour, thus meets the demand at cooling decompression station.
Improvement in this way, have great energy conservation and environmental protection meaning, can not have to additionally reuse boiler come it is soft
Water.
Claims (8)
1. a kind of continuous boiling pan draining system of brown sugar, comprising:
Pedestal；
Upper water box, the upper water box are fixedly installed at the top of the pedestal；
Boiling pan, the boiling pan include an effect boiling pan and two effect boiling pans, and the effect boiling pan is installed on the pedestal
Upper and be located at below the upper water box, effect boiling pan bottom is equipped with the first steam chest, first steam chest be equipped with first into
Steam ports and the first venthole, the two effects boiling pan is installed on the pedestal and is located at below the effect boiling pan, described
Two effect boiling pan bottoms are equipped with the second steam chest, and second steam chest is equipped with the second air intake and the second venthole, and two effect is boiled
Conveying pipeline is equipped between sugar bowl and the effect boiling pan, the discharge port of the two effects boiling pan connects massecuite separator；
Heating plant, it is the first steam chest steam supply that the heating plant, which connects first air intake,；It is characterized in that, also wrapping
It includes:
Water circle device, the water circle device include intermediate water tank, lower header, water pump, the first steam-water separator and second
Steam-water separator, the intermediate water tank is installed on the pedestal and is located at sustained height with the two effects boiling pan, under described
Water tank is set to below the two effects boiling pan, and first venthole passes through the air intake of pipeline and first steam-water separator
The water outlet of connection, first steam-water separator is connect by pipeline with the water inlet of the intermediate water tank, the intermediate water
The water outlet of case is connect by pipeline with the water inlet of the lower header, is equipped between the intermediate water tank and the heating plant
The water outlet of water-supply-pipe, the lower header connects the upper water box by pipeline, and the water pump is installed on the lower header and institute
State for the water in the lower header to be pumped into the upper water box between upper water box, second venthole by pipeline with it is described
The air intake of second steam-water separator connects, and the water outlet of second steam-water separator connects the lower header by pipeline
Water inlet.
2. the continuous boiling pan draining system of brown sugar as described in claim 1, which is characterized in that the first steam-water separator packet
The first steam-water separation cylinder is included, is equipped with venthole at the top of the first steam-water separation cylinder, the first steam-water separation cylinder side is equipped with
For being connected to the air intake of first steam chest, the first steam-water separation cylinder bottom is taper and is equipped with water outlet；Described
Two steam-water separators include the second steam-water separation cylinder, are equipped with venthole, second steam-water separation at the top of the second steam-water separation cylinder
Cylinder side is equipped with the air intake for being connected to second steam chest, and the second steam-water separation cylinder bottom is taper and is equipped with water outlet
Mouthful.
3. the continuous boiling pan draining system of brown sugar as claimed in claim 2, which is characterized in that the first steam-water separation cylinder and
The height of the second steam-water separation cylinder is 0.8~1.2 meter, the first steam-water separation cylinder and the second steam-water separation cylinder
Equal 0.24~0.26 meter of internal diameter.
4. the continuous boiling pan draining system of brown sugar as claimed in claim 3, which is characterized in that the first steam-water separation cylinder side
The distance of the air intake in portion venthole at the top of the first steam-water separation cylinder is greater than 0.5 meter；The second steam-water separation cylinder
The distance of the air intake of side venthole at the top of the second steam-water separation cylinder is greater than 0.5 meter.
5. the continuous boiling pan draining system of brown sugar as claimed in claim 4, which is characterized in that it further include agitating device, it is described
Agitating device includes agitating shaft, stirring motor, bearing block and stirring blade, and the agitating shaft extends transversely through an effect and boils sugar
Tank is respectively equipped with sealing device between the both ends of the agitating shaft and the effect boiling pan, and the both ends of the agitating shaft are in institute
It states and is respectively equipped with the bearing block outside an effect boiling pan, two bearing blocks are individually fixed on the effect boiling pan,
The agitating shaft and the stirring motor are sequentially connected, and the stirring blade is set in the effect boiling pan and is installed on described
On agitating shaft.
6. the continuous boiling pan draining system of brown sugar as claimed in claim 5, which is characterized in that it further include temperature measuring equipment, it is described
One effect boiling pan left side be equipped with feed inlet, it is described one effect boiling pan lower right side be equipped with discharge port, the feed inlet with
Multiple first steam chests are equipped between the discharge port, the temperature measuring equipment includes temperature probe and display, an effect
In being respectively equipped with the temperature probe, each temperature probe on the lateral wall of each first steam chest in boiling pan
The display is connected by thermometric line, the thermometric line outer cover is equipped with steel pipe, and the steel pipe is fixed on an effect and boils sugar
On the inner sidewall of tank.
7. the continuous boiling pan draining system of brown sugar as claimed in claim 6, which is characterized in that the heating plant includes boiler
With cooling decompression station, first air intake connects the cooling decompression station by pipeline, and the cooling decompression station passes through pipeline
The boiler is connected, the steam that the boiler generates is by being passed through first steam chest, the centre behind the cooling decompression station
Water tank connects cooling decompression station by water-supply-pipe and supplies water for it.
8. the continuous boiling pan draining system of brown sugar as claimed in claim 7, which is characterized in that the two effects boiling pan, which is equipped with, to be stirred
Mix device and temperature measuring equipment.
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| CN110106292B (en) | 2023-10-27 |
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Address after: 536015 Fucheng Town, Yinhai District, Beihai City, Guangxi Zhuang Autonomous Region Applicant after: Guangxi sugar group Xingxing Sugar Co.,Ltd. Address before: 536015 Fucheng Town, Yinhai District, Beihai City, Guangxi Zhuang Autonomous Region Applicant before: GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP XINGXING SUGAR PRODUCTION CO.,LTD. |
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