CN209341686U - Vinasse albumen Feed Manufacturing Air Dried System - Google Patents
Vinasse albumen Feed Manufacturing Air Dried System Download PDFInfo
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- CN209341686U CN209341686U CN201822198705.5U CN201822198705U CN209341686U CN 209341686 U CN209341686 U CN 209341686U CN 201822198705 U CN201822198705 U CN 201822198705U CN 209341686 U CN209341686 U CN 209341686U
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 239000005457 ice water Substances 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 239000000463 material Substances 0.000 claims abstract description 30
- 238000001035 drying Methods 0.000 claims abstract description 25
- 125000004122 cyclic group Chemical group 0.000 claims abstract description 19
- 238000012856 packing Methods 0.000 claims abstract description 15
- 230000008676 import Effects 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 93
- 239000003599 detergent Substances 0.000 claims description 27
- 238000004140 cleaning Methods 0.000 claims description 15
- 238000010926 purge Methods 0.000 claims description 12
- 238000011010 flushing procedure Methods 0.000 claims description 10
- 238000009833 condensation Methods 0.000 claims description 7
- 230000005494 condensation Effects 0.000 claims description 7
- 238000010079 rubber tapping Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 238000004064 recycling Methods 0.000 claims description 4
- 238000004806 packaging method and process Methods 0.000 claims description 2
- 238000009423 ventilation Methods 0.000 claims 1
- 230000005540 biological transmission Effects 0.000 abstract description 10
- 239000000428 dust Substances 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000013590 bulk material Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
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- Drying Of Gases (AREA)
Abstract
The utility model relates to a kind of vinasse albumen Feed Manufacturing Air Dried Systems, the feed inlet of the discharge port connection cyclic conveyor of dry discharger, the feed inlet of the discharge port connection feeder of cyclic conveyor, the discharge gate of cyclic conveyor is connected to crushing packing system, the air inlet of the gas outlet connection air-introduced machine of dry discharger, the hot air intake of the gas outlet connection cold air heat exchanger of air-introduced machine, the air inlet of the heat outlet connection ice water heat exchanger of cold air heat exchanger, the feed inlet of the discharge port connection gas-liquid separator of ice water heat exchanger, the cold wind import of the gas outlet connection cold air heat exchanger of gas-liquid separator, the liquid outlet connection of gas-liquid separator is condensed back to closed cans, the cold wind outlet air blower of cold air heat exchanger, air blower is connected to the discharge port of heater connection feeder, wet stock is carried by the air of high temperature drying Wind send transmission, absorbs the moisture content in material in the dry air of transmission process high temperature, achievees the purpose that material is dried.
Description
Technical field
The utility model relates to the powders such as vinasse albumen feed, the conveying of particulate species bulk material and cooling equipment and technologies
A kind of field, and in particular to vinasse albumen Feed Manufacturing Air Dried System.
Background technique
In alcohol production process, after fermentation liquid distills out alcohol, the wine lees liquor rich in protein, wine lees liquor can be left
At filter residue and filtrate two parts after being separated by solid-liquid separation, wherein filter residue is vinasse, and vinasse can be used for after pipe bundle drier is dry
Full vinasse drying feed is produced, and filtrate is also fed to drying machine drying after being concentrated by evaporation, the product after drying can also be used for
Produce full vinasse drying feed.Currently, what is generallyd use to the drying of filter residue is pipe bundle drier, pipe bundle drier is with high temperature
Steam is heat source, and high-temperature steam enters in the heat-exchanging tube bundle of pipe bundle drier, is carried out with the intracorporal material of shell of pipe bundle drier
Heat exchange, material are dried, and high-temperature steam cooling condensation, in the process, the tube core of pipe bundle drier constantly rotates, by object
Material is carried to the eminence of tube bank drier, and then free-falling carries out heat exchange between the tube bank of pipe bundle drier, and tube bank is dry
The dry general volume of machine is larger, and length is longer, and power needed for tube core rotates is larger, moreover, because the heat exchanger tube one of composition tube bank
As length it is longer, and in order to guarantee that heat exchange efficiency, the wall thickness of heat exchanger tube are relatively thin, use, the easy sagging deflections of heat exchanger tube, hold for a long time
Heat exchanger tube wear and rupture is easily caused, causes pipe bundle drier operating cost high, equipment investment is big, and frequently, service life is short for maintenance,
Seriously affect the production efficiency of vinasse albumen feed.
Utility model content
In conclusion in order to overcome the shortcomings of that prior art problem, the utility model provide a kind of vinasse albumen feed
Production Air Dried System, it is to carry wet stock wind by the air of high temperature drying to send transmission, in transmission process high temperature
Dry air absorbs the moisture content in material, achievees the purpose that material is dried.
In order to solve the above technical problems, the technical solution adopted by the utility model is:
A kind of vinasse albumen Feed Manufacturing Air Dried System, in which: defeated including feeder, dry discharger, circulation
It send machine, air-introduced machine, cold air heat exchanger, ice water heat exchanger, gas-liquid separator, be condensed back to closed cans, air blower, heater and crushing
Packaging system, the feed inlet of the feeder are connected to wet stock source, and the discharge port of the feeder connects dry discharger
Feed inlet, the feed inlet of the discharge port connection cyclic conveyor of dry discharger, the discharge port of the cyclic conveyor connects
The feed inlet of feeder is connect, the discharge gate of cyclic conveyor is connected to crushing packing system, the gas outlet of the drying discharger
It is connected to the air inlet of air-introduced machine, the hot air intake of the gas outlet connection cold air heat exchanger of air-introduced machine, the cold air heat exchange
The air inlet of the heat outlet connection ice water heat exchanger of device, the feed inlet of the discharge port connection gas-liquid separator of ice water heat exchanger,
The cold wind import of the gas outlet connection cold air heat exchanger of the gas-liquid separator, the liquid outlet of the gas-liquid separator connect
The logical inlet for being condensed back to closed cans, the air inlet of the cold wind outlet air blower of the cold air heat exchanger, air blower
Gas outlet is connected to the air inlet of heater, the discharge port of the gas outlet connection feeder of heater, the cold air heat exchanger
Condensation-water drain connection be condensed back to the inlet of closed cans, the liquid outlet for being condensed back to closed cans passes through condensing recovery pump connection
Mash destilling tower, the ice water import of the ice water heat exchanger and ice water outlet are respectively communicated with the water outlet and return water in ice water source
Mouthful.
Further, the crushing packing system include pulverizer, wind send discharger, wind send deduster, wind pressure fan, at
Product sieve, feed bin and packing machine, the feed inlet of the pulverizer are connected to the discharge gate of cyclic conveyor, the discharge port of pulverizer
The feed inlet for sending pipeline connection wind to send discharger by wind, wind send the air outlet of discharger to be connected to the air inlet that wind send deduster,
The gas outlet of the air inlet that wind send the gas outlet of deduster to be connected to wind pressure fan, wind pressure fan is connected to atmosphere, and wind send discharger
Discharge port and wind send the discharge port of deduster to be connected to the feed inlet of finished product screen, the charging of the discharge port connection feed bin of finished product screen
Mouthful, the discharge port of feed bin connects packing machine.
Further, the ice water heat exchanger and cold air heat exchanger connect cleaning system, and the cleaning system includes
Washwater tank and flushing water pump, the water inlet of the water outlet connection flushing water pump of washwater tank, the water outlet of flushing water pump pass through
First detergent line, the second detergent line and third detergent line are respectively communicated with the discharge port of ice water heat exchanger, cold air heat exchange
The Butterworth Hatch of device and the condensation-water drain of cold air heat exchanger, the first detergent line, the second detergent line and third detergent line
On be respectively set the first purge valve, the second purge valve and third purge valve, the air inlet of the ice water heat exchanger passes through first
Water return pipeline is connected to return main, and the gas outlet of the cold air heat exchanger is connected to return main by the second water return pipeline,
The cleaning water outlet of the cold air heat exchanger is connected to return main by third water return pipeline, on the first water return pipeline, the
The first back-water valve (BWV), the second back-water valve (BWV) and third back-water valve (BWV), return main are respectively set on two water return pipelines, on third water return pipeline
It is connected to the water return outlet of washwater tank.
Further, on the pipeline that the condensation-water drain of the cold air heat exchanger is connected to the inlet for being condensed back to closed cans
It is provided with tapping valve, the tapping valve is arranged on the pipeline between the inlet for being condensed back to closed cans and third detergent line.
Further, it is provided on the pipeline that the liquid outlet of ice water heat exchanger is connected to the feed inlet of gas-liquid separator
Outlet valve.
Further, the drying discharger is whirlwind discharger, is provided with wind stopping device on discharge port.
Further, it is whirlwind discharger that the wind, which send discharger and wind to send deduster, and wind send discharger and wind to send and removes
Wind stopping device is provided on the discharge port of dirt device.
The utility model has the following beneficial effects:
1, the utility model is to carry wet stock wind by the air of high temperature drying to send transmission, dry in transmission process high temperature
Dry air absorbs the moisture content in material, achievees the purpose that material is dried, compared with existing pipe bundle drier, this reality
Air after being heating with the novel drying source to wet stock, for the high-temperature steam of pipe bundle drier, high temperature is empty
Gas is easier to be made, and energy consumption is few, moreover, the equipment that the utility model uses is only tubular heat exchanger and whirlwind discharging
Device, equipment is simple, manufacturing cost is low, and the utility model can effectively improve dry effect using air-supply transmission, efficiency of transmission height
Rate, therefore, when the utility model can be effectively solved existing vinasse albumen Feed Manufacturing, whens vinasse dry materials is existing to be set
The problems such as standby investment is high, and drying efficiency is low, drying cost is high.
2, the utility model setting cold air heat exchanger and ice water heat exchanger, the air of high temperature drying are carried out to wet stock
When dry, wind send during other than taking away the moisture content in wet stock, part particulate dust can be also carried away, moreover, in moisture content
There are alcohol, the air themperature of high temperature drying is reduced, and humidity increases, and contains material, and therefore, the gas after drying is not easy to arrange
It puts, the air cooling-down after the utility model keeps participation dry by cold air heat exchanger condenses, and so that air is become drying again, and
Particulate dust in condensation process in air is condensed recycling, and air enters ice water heat exchanger later, and air is further
Condensation cooling, air become cold air, which participates in the heat exchange in cold air heat exchanger, and cold air tentatively heats up laggard
Enter the drying participated in after heater heats to wet stock, is discharged in whole process without gas, air circulation uses, energy-saving and emission-reduction.
3, cleaning system is arranged in the utility model, and cleaning system can carry out cold air heat exchanger 5 and ice water heat exchanger 6
Wash cycles, for the air of high temperature drying after wet stock is dried, the particulate dust carried in air is entering heat exchanger
Afterwards, in air setting heat transfer process, particulate dust can bond in the shell and heat exchanger tube of heat exchanger, influence heat exchange efficiency effect
The stable operation of fruit and equipment, the setting of cleaning system, can heat exchanging device cleaned, the material of bonding is cleared up,
Guarantee the stable operation of heat exchange efficiency, heat transfer effect and equipment.
4, crushing packing system is arranged in the utility model, and the material after drying enters the laggard inlet air of pulverizer crushing and send discharging
Device rewinding send deduster dedusting rewinding into wind, and material recycle is sufficiently thorough, while blast system meeting during material transferring
Wind is carried out to the material after dry heating and send cooling, reduces temperature of charge, it is dry that the setting of pulverizer can be effectively solved material
Material during dry due to moisture evaporates caused by the blocking problem of materials from bonding, send cooling and material to return convenient for subsequent wind
It receives, the granularity of material is made to meet Feed Manufacturing needs.
5, the condensed water of recycling is delivered to mash steaming by condensing recovery pump by the closed cans that is condensed back to of the utility model again
Tower is evaporated, because containing particulate dust in condensed water, can be realized the recycling to particulate dust.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawing.
As shown in Figure 1, a kind of vinasse albumen Feed Manufacturing Air Dried System, including feeder 1, dry discharger 2,
Cyclic conveyor 3, cold air heat exchanger 5, ice water heat exchanger 6, gas-liquid separator 7, is condensed back to closed cans 8, air blower at air-introduced machine 4
9, the feed inlet of heater 10 and crushing packing system, the feeder 1 is connected to wet stock source 11, the feeder 1
Discharge port connects the feed inlet of dry discharger 2, and the feed inlet of the discharge port connection cyclic conveyor 3 of dry discharger 2 is dry
Discharger 2 is whirlwind discharger, and wind stopping device is provided on discharge port, and the discharge port of the cyclic conveyor 3 connects feeding
The discharge gate of the feed inlet of device 1, cyclic conveyor 3 is connected to crushing packing system, and the crushing packing system includes pulverizer
14, wind send discharger 15, wind to send deduster 16, wind pressure fan 17, finished product screen 18, feed bin 19 and packing machine 20, the crushing
The feed inlet of machine 14 is connected to the discharge gate of cyclic conveyor 3, and the discharge port of pulverizer 14 send pipeline connection wind to send and unloads by wind
The feed inlet of glassware 15, wind send the air outlet of discharger 15 to be connected to the air inlet that wind send deduster 16, and wind send going out for deduster 16
Port is connected to the air inlet of wind pressure fan 17, and the gas outlet of wind pressure fan 17 is connected to atmosphere, wind send discharger 15 discharge port and
Wind send the discharge port of deduster 16 to be connected to the feed inlet of finished product screen 18, the charging of the discharge port connection feed bin 19 of finished product screen 18
Mouthful, the discharge port of feed bin 19 connects packing machine 20.
The air inlet of the gas outlet connection air-introduced machine 4 of dry discharger 2, the gas outlet connection cold air heat exchange of air-introduced machine 4
The hot air intake of device 5, the air inlet of the heat outlet connection ice water heat exchanger 6 of the cold air heat exchanger 5, ice water heat exchanger
The feed inlet of 6 discharge port connection gas-liquid separator 7, the liquid outlet of ice water heat exchanger 6 are connected to the feed inlet of gas-liquid separator 7
Pipeline on be provided with outlet valve 37, the cold wind import of the gas outlet connection cold air heat exchanger 5 of the gas-liquid separator 7,
The liquid outlet connection of the gas-liquid separator 7 is condensed back to the inlet of closed cans 8, and the cold wind of the cold air heat exchanger 5 goes out
The air inlet of mouth connection air blower 9, the air inlet of the gas outlet connection heater 10 of air blower 9, the gas outlet of heater 10 connects
The discharge port of logical feeder 1, the condensation-water drain connection of the cold air heat exchanger 5 is condensed back to the inlet of closed cans 8, described
The liquid outlet for being condensed back to closed cans 8 by 12 connection mash destilling towers of condensing recovery pump, the ice water of the ice water heat exchanger 6 into
Mouth and ice water outlet are respectively communicated with the water outlet and water return outlet in ice water source 13.The wind send discharger 15 and wind to send deduster 16
It is whirlwind discharger, wind send discharger 15 and wind to send on the discharge port of deduster 16 and is provided with wind stopping device.
The ice water heat exchanger 6 and cold air heat exchanger 5 connect cleaning system, and the cleaning system includes ejected wash water
Tank 21 and flushing water pump 22, the water inlet of the water outlet connection flushing water pump 22 of washwater tank 21, the water outlet of flushing water pump 22
By the first detergent line 23, the second detergent line 24 and third detergent line 25 be respectively communicated with ice water heat exchanger 6 discharge port,
The Butterworth Hatch of cold air heat exchanger 5 and the condensation-water drain of cold air heat exchanger 5, the first detergent line 23, the second detergent line
24 and third detergent line 25 on the first purge valve 26, the second purge valve 27 and third purge valve 28, the ice is respectively set
The air inlet of water- to-water heat exchanger 6 is connected to return main 30, the gas outlet of the cold air heat exchanger 5 by the first water return pipeline 29
It is connected to return main 30 by the second water return pipeline 31, the cleaning water outlet of the cold air heat exchanger 5 passes through third return water
Pipeline 32 is connected to return main 30, sets respectively on the first water return pipeline 29, on the second water return pipeline 31, on third water return pipeline 32
The first back-water valve (BWV) 33, the second back-water valve (BWV) 34 and third back-water valve (BWV) 35 are set, return main 30 is connected to the water return outlet of washwater tank 21.
It is arranged on the pipeline that the condensation-water drain of the cold air heat exchanger 5 is connected to the inlet for being condensed back to closed cans 8
There is tapping valve 36, the pipeline between the inlet for being condensed back to closed cans 8 and third detergent line 25 is arranged in the tapping valve 36
On.
In use, vinasse enter feeder 1, start air-introduced machine 4 and air blower 9, dry sky under the action of air blower 9
Gas enters heater 10 and is heated into high temperature dry air, and under the action of air-introduced machine 4, high temperature dry air provides feeder 1
Vinasse wet stock carry out wind and send transmission, send wet stock in transmission process to be dried in wind, and enter dry discharger 2, drying
Material enter cyclic conveyor 3 from the discharge port of dry discharger 2, the material after a part is dry by cyclic conveyor 3 again
Secondary to be delivered to feeder 1 and wet stock mixing, for wet stock by preliminarily dried, the material after another part is dry enters pulverizer
14 crush after sent by wind to wind discharger 15 sent to carry out material collection, the cooled cooling of material during wind is sent, wind send air into
Inlet air discharges after sending 16 dedusting of deduster, and the dried material of collection enters feed bin 19 after the screening of finished product screen 18, is packaged later.
High temperature dry air into dry discharger 2 absorbs the moisture content in wet stock and carries part particulate dust, from dry discharging
The air outlet of device 2 flows out, and cold air heat exchanger 5 is entered under the action of air-introduced machine 4, with the cold sky for entering cold air heat exchanger 5
Gas carries out heat exchange, and cold air heat exchanger 5 is tubular heat exchanger, and the hot-air flowed out from dry discharger 2 enters tubulation heat exchange
In the heat exchanger tube of device, tube side flow, cold air enters in the shell of tubular heat exchanger, shell fluid flow.Hot-air is changed with cold air
It after heat, is flowed out after hot-air cooling condensation from the upper end gas outlet of cold air heat exchanger 5, into ice water heat exchanger 6, ice water heat exchange
Device 6 is also tubular heat exchanger, and ice water enters in the heat exchanger tube of tubular heat exchanger, and tube side flow, hot-air enters tubular heat exchanger
Shell in, shell fluid flow, ice water and air heat exchange, hot-air becomes cold air by cooling condensation again, cold air with
Condensed water enters the separation of gas-liquid separator 7 together, and cold air is transported to the inlet of cold air of cold air heat exchanger 5, shell side stream
It is dynamic, in cold air heat exchanger 5, after cold air and hot air heat exchange, after cold air heating, enter heater through air blower 9
10 heating, participate in sending drying to the wind of vinasse wet stock again.
The condensed water that condensed water and gas-liquid separator 7 are isolated in cold air heat exchanger 5, which enters, is condensed back to closed cans 8, due to
Contain particulate dust and alcohol in condensed water, therefore, under the action of condensing recovery pump 12, is transported to mash destilling tower again
Carry out alcohol distillation.
After system runs a period of time, since the particulate dust that condenses in condensation process can be in ice water heat exchanger 6 and cold
Bonding in air heat exchanger 5, therefore, it is necessary to clean to ice water heat exchanger 6 and cold air heat exchanger 5.At this point, closing drain
Valve 36 and outlet valve 37 open flushing water pump 22, the first purge valve 26, the second purge valve 27, third purge valve 28, the first return water
Valve 33, the second back-water valve (BWV) 34 and third back-water valve (BWV) 35, the ejected wash water in washwater tank 21 under the action of flushing water pump 22 respectively
Ejected wash water pair into the first detergent line 23, the second detergent line 24 and third detergent line 25, in the first detergent line 23
The shell of ice water heat exchanger 6 is cleaned, i.e. cleaning in shell-side, and ejected wash water enters return main 30 from the first water return pipeline 29, the
Ejected wash water in two detergent lines 24 cleans the shell of cold air heat exchanger 5, i.e. cleaning in shell-side, and ejected wash water is returned from third
Water lines 32 enter return main 30, and the ejected wash water in third detergent line 25 carries out the heat exchanger tube of cold air heat exchanger 5 clear
It washes, i.e., tube side cleans, and ejected wash water enters return main 30 from the second water return pipeline 31, and the ejected wash water in return main 30 enters clear
Wash water tank 21 so far completes the cleaning to ice water heat exchanger 6 and cold air heat exchanger 5.
Connecting pipeline between the gas outlet of the cold air heat exchanger 5 of the utility model and the air inlet of ice water heat exchanger 6
On be provided with control valve 38, the control valve 38 is arranged between the first water return pipeline 29 and the second water return pipeline 31, to object
When material is dried, control valve 38 is opened, and when heat exchanging device is cleaned, control valve 38 is closed.
It should be noted that embodiment described above be to the illustrative and not limiting of technical solutions of the utility model, it is affiliated
The equivalent replacement of technical field those of ordinary skill or the other modifications made according to the prior art, as long as unpractical beyond this
The thinking and range of new technique scheme, should be included within interest field required by the utility model.
Claims (7)
1. a kind of vinasse albumen Feed Manufacturing Air Dried System, it is characterised in that: including feeder (1), dry discharger
(2), cyclic conveyor (3), air-introduced machine (4), cold air heat exchanger (5), ice water heat exchanger (6), gas-liquid separator (7), condensation
The feed inlet of recycling can (8), air blower (9), heater (10) and crushing packing system, the feeder (1) is connected to wet object
Material source (11), the discharge port of the feeder (1) connect the feed inlet of dry discharger (2), the discharging of dry discharger (2)
The feed inlet of mouth connection cyclic conveyor (3), the feed inlet of discharge port connection feeder (1) of the cyclic conveyor (3),
The discharge gate of cyclic conveyor (3) is connected to crushing packing system, and the gas outlet of the drying discharger (2) is connected to air-introduced machine
(4) air inlet, the hot air intake of gas outlet connection cold air heat exchanger (5) of air-introduced machine (4), the cold air heat exchanger
(5) discharge port of the air inlet of heat outlet connection ice water heat exchanger (6), ice water heat exchanger (6) is connected to gas-liquid separator (7)
Feed inlet, the gas-liquid separator (7) gas outlet connection cold air heat exchanger (5) cold wind import, the gas-liquid
The liquid outlet connection of separator (7) is condensed back to the inlet of closed cans (8), and the cold wind of the cold air heat exchanger (5), which exports, to be connected
The air inlet of logical air blower (9), the air inlet of gas outlet connection heater (10) of air blower (9), the outlet of heater (10)
The condensation-water drain connection of the discharge port of mouth connection feeder (1), the cold air heat exchanger (5) is condensed back to closed cans (8)
Inlet, the liquid outlet for being condensed back to closed cans (8) are connected to mash destilling tower, the ice water by condensing recovery pump (12)
The ice water import of heat exchanger (6) and ice water outlet are respectively communicated with the water outlet and water return outlet in ice water source (13).
2. vinasse albumen Feed Manufacturing Air Dried System according to claim 1, it is characterised in that: the crushing
Packaging system include pulverizer (14), wind send discharger (15), wind send deduster (16), wind pressure fan (17), finished product screen (18),
The feed inlet of feed bin (19) and packing machine (20), the pulverizer (14) is connected to the discharge gate of cyclic conveyor (3), is crushed
The feed inlet that the discharge port of machine (14) send pipeline connection wind to send discharger (15) by wind, wind send the air outlet of discharger (15) to connect
The air inlet of deduster (16), the air inlet that wind send the gas outlet of deduster (16) to be connected to wind pressure fan (17) are sent in ventilation, and wind is sent
The gas outlet of blower (17) is connected to atmosphere, wind send the discharge port of discharger (15) and wind send the discharge port of deduster (16) at
Product sieve the feed inlet connection of (18), the feed inlet of discharge port connection feed bin (19) of finished product screen (18), the discharge port of feed bin (19)
It connects packing machine (20).
3. vinasse albumen Feed Manufacturing Air Dried System according to claim 1, it is characterised in that: the ice water
Heat exchanger (6) and cold air heat exchanger (5) connect cleaning system, and the cleaning system includes washwater tank (21) and ejected wash water
It pumps (22), the water inlet of water outlet connection flushing water pump (22) of washwater tank (21), the water outlet of flushing water pump (22) passes through
First detergent line (23), the second detergent line (24) and third detergent line (25) are respectively communicated with going out for ice water heat exchanger (6)
The condensation-water drain of material mouth, the Butterworth Hatch of cold air heat exchanger (5) and cold air heat exchanger (5), the first detergent line (23),
The first purge valve (26), the second purge valve (27) and third are respectively set in two detergent lines (24) and third detergent line (25)
The air inlet of purge valve (28), the ice water heat exchanger (6) passes through the first water return pipeline (29) connection return main (30), institute
The gas outlet for the cold air heat exchanger (5) stated passes through the second water return pipeline (31) connection return main (30), the cold air
The cleaning water outlet of heat exchanger (5) is connected to return main (30) by third water return pipeline (32), on the first water return pipeline (29),
Be respectively set on second water return pipeline (31), on third water return pipeline (32) the first back-water valve (BWV) (33), the second back-water valve (BWV) (34) and
Third back-water valve (BWV) (35), return main (30) are connected to the water return outlet of washwater tank (21).
4. vinasse albumen Feed Manufacturing Air Dried System according to claim 3, it is characterised in that: the cold sky
Tapping valve (36), institute are provided on the pipeline that the condensation-water drain of gas heat exchanger (5) is connected to the inlet for being condensed back to closed cans (8)
The tapping valve (36) stated is arranged on the pipeline being condensed back between the inlet of closed cans (8) and third detergent line (25).
5. vinasse albumen Feed Manufacturing Air Dried System according to claim 1, it is characterised in that: the ice water
Outlet valve (37) are provided on the pipeline that the liquid outlet of heat exchanger (6) is connected to the feed inlet of gas-liquid separator (7).
6. vinasse albumen Feed Manufacturing Air Dried System according to claim 1, it is characterised in that: the drying
Discharger (2) is whirlwind discharger, is provided with wind stopping device on discharge port.
7. vinasse albumen Feed Manufacturing Air Dried System according to claim 2, it is characterised in that: the wind is sent
It is whirlwind discharger, the discharging that wind send discharger (15) and wind to send deduster (16) that discharger (15) and wind, which send deduster (16),
Wind stopping device is provided on mouthful.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822198705.5U CN209341686U (en) | 2018-12-26 | 2018-12-26 | Vinasse albumen Feed Manufacturing Air Dried System |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822198705.5U CN209341686U (en) | 2018-12-26 | 2018-12-26 | Vinasse albumen Feed Manufacturing Air Dried System |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209341686U true CN209341686U (en) | 2019-09-03 |
Family
ID=67759021
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822198705.5U Withdrawn - After Issue CN209341686U (en) | 2018-12-26 | 2018-12-26 | Vinasse albumen Feed Manufacturing Air Dried System |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209341686U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109489345A (en) * | 2018-12-26 | 2019-03-19 | 郑州博大浓缩干燥设备有限公司 | Vinasse albumen Feed Manufacturing Air Dried System |
| CN112197514A (en) * | 2020-10-26 | 2021-01-08 | 湖南精诚制药机械有限公司 | Vacuum drying oven that likepowder medicament is dry with drying efficiency height |
-
2018
- 2018-12-26 CN CN201822198705.5U patent/CN209341686U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109489345A (en) * | 2018-12-26 | 2019-03-19 | 郑州博大浓缩干燥设备有限公司 | Vinasse albumen Feed Manufacturing Air Dried System |
| CN109489345B (en) * | 2018-12-26 | 2024-01-30 | 郑州博大浓缩干燥设备有限公司 | Air flow drying system for distillers' grains protein feed production |
| CN112197514A (en) * | 2020-10-26 | 2021-01-08 | 湖南精诚制药机械有限公司 | Vacuum drying oven that likepowder medicament is dry with drying efficiency height |
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