CN207227373U - A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment - Google Patents
A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment Download PDFInfo
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- CN207227373U CN207227373U CN201721438493.2U CN201721438493U CN207227373U CN 207227373 U CN207227373 U CN 207227373U CN 201721438493 U CN201721438493 U CN 201721438493U CN 207227373 U CN207227373 U CN 207227373U
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Abstract
The utility model discloses a kind of extraction of plant medicinal liquid and Activated Carbon Production process equipment, including fruit stone to fumigate vaporization extraction system, activated carbon production system and activated carbon system of processing；The fruit stone is fumigated vaporization extraction system, activated carbon production system and activated carbon system of processing and is sequentially connected；The fruit stone, which fumigates vaporization extraction system, includes raw material cabin, the first helical feeder, stifling gasification burner, intermediate bin, the first condenser, the first cooling-water machine, the first pump, medicine original fluid container and the first wind turbine；The activated carbon production system includes the second helical feeder, activation furnace, the second wind turbine, the 3rd wind turbine, steam oven, the second condenser, the second cooling-water machine, the second pump and secondary medicine stoste and fills.The equipment prepares fractional oil of haw kernel co-production activated carbon by raw material of Chinese hawthorn seed, realizes the comprehensive utilization of resource, avoids only focusing on production single product and ignoring the economic value of byproduct.
Description
Technical field
The utility model belongs to edible fruit stone processing technique field, is specifically a kind of plant medicinal liquid extraction and Activated Carbon Production
Process equipment.
Background technology
Fruit stone is wrapped in the duricrust part of seed as fruit center, there is abundant resource in China, but various fruits
Pile up like a mountain for the cannery in the place of production or the fruit stone of fruit wine factory, there is no and is developed and utilized, and substantial amounts of fruit stone is as useless
Thing processing, causes the pollution of environment.Modern science and technology method has confirmed there is good antibacterial from the juice of fruit stone extraction, kills
The effect of bacterium and disinfection, and medical and health, food processing and each field of environmental protection are had been widely used for, such as the mountain by purification
Short, bristly hair or beard core evaporates oil and is configured to ointment and creme, and treating the illnesss such as eczema, neurodermatitis, burn has the effect of obvious, while it is right
Nine kinds of bacteriums such as Escherichia coli have obvious inhibitory action.In addition, Chinese hawthorn seed is used directly as Chinese medicine, hernia can be treated
The diseases such as gas, difficult labour.
The utilization of Chinese hawthorn seed at present is mostly that Chinese hawthorn seed is placed in reaction kettle, isolation air heating, with the rising of temperature
Flue gas spilling is had, Chinese hawthorn seed fraction can be obtained by by condenser condensation, remaining solid thing is rough Chinese hawthorn seed charcoal.Application
Numbers 201320817197.9 disclose a kind of activation fluidized bed furnace for producing activated carbon, it is by activation furnace body and auxiliary device group
Into activation furnace body includes burner hearth, insulating layer, air inlet pipe, feed inlet, discharge port, thermometer hole and peep hole.It uses gaseous mixture
Body stirs the material in stove so that material can be stirred equably, come into full contact with high temperature with vapor, ensure activation
Uniformly.The device uses single process, extracts single material, produces single product, without reference to raw material and product
Coproduction and comprehensive utilization of resources, sufficiently do not form complete process system using raw material, it is impossible to comprehensively utilize and make
Cost improves.
Utility model content
In view of the deficiencies of the prior art, the technical problem that the utility model intends to solve is to provide a kind of plant medicinal liquid extraction
With Activated Carbon Production process equipment.The equipment prepares fractional oil of haw kernel co-production activated carbon by raw material of Chinese hawthorn seed, realizes money
The comprehensive utilization in source, avoids only focusing on production single product and ignoring the economic value of byproduct.In the process of Chinese hawthorn seed pyrolysis
Heat is provided in the fuel gas circulating involuting system of middle generation, realizes the saving of raw material resources, reduces the pollution to environment.
The technical solution that the utility model solves the technical problem is to provide a kind of plant medicinal liquid extraction and activated carbon life
Produce process equipment, including activated carbon system of processing, it is characterised in that the equipment further includes fruit stone and fumigates vaporization extraction system and work
Property charcoal production system；The fruit stone is fumigated vaporization extraction system, activated carbon production system and activated carbon system of processing and is sequentially connected；
The fruit stone fumigate vaporization extraction system include raw material cabin, the first helical feeder, stifling gasification burner, intermediate bin,
First condenser, the first cooling-water machine, the first pump, medicine original fluid container and the first wind turbine；The raw material cabin and the first helical feeder
One end connects；The other end of first helical feeder is connected with the material inlet of stifling gasification burner；The stifling vaporization
The gas entry of stove is connected with extraneous gas pipeline；The discharge port of the stifling gasification burner is connected with intermediate bin；It is described smoked
The evaporation exhanst gas outlet for steaming gasification burner is connected by pipeline with the condensation tube inlet of the first condenser；First condenser it is cold
Condensate outlet is connected with the first cooling-water machine；First cooling-water machine is connected by the condensing water inlet of the first pump and the first condenser
Connect；The condenser pipe outlet of first condenser is connected by pipeline with medicine original fluid container；The condenser pipe of first condenser goes out
The side wall of mouth vertical pipeline is connected by the first wind turbine with the gas returning port of stifling gasification burner；
The activated carbon production system include the second helical feeder, activation furnace, the second wind turbine, the 3rd wind turbine, steam oven,
Second condenser, the second cooling-water machine, the second pump and secondary medicine stoste fill；One end of second helical feeder connects with intermediate bin
Connect, the material inlet connection of the other end and activation furnace；The gas entry of the activation furnace is connected with extraneous gas pipeline；
The steam entry of the activation furnace is connected by pipeline with extraneous oxygen and steam oven, and the second wind turbine is provided with pipeline；Institute
The gas outlet side for stating activation furnace is connected by pipeline and activation air valve with the 3rd wind turbine, and the gas outlet opposite side of activation furnace passes through
Pipeline and evaporation smoke valve are connected with the condensation tube inlet of the second condenser；The gas returning port of 3rd wind turbine and stifling gasification burner
Connection；The condensation-water drain of second condenser is connected with the second cooling-water machine；Second cooling-water machine passes through the second pump and the
The condensing water inlet connection of two condensers；The condenser pipe outlet of second condenser passes through vertical pipeline and secondary medicine original fluid container
Connection.
Compared with prior art, the utility model beneficial effect is：
(1) the utility model co-producing active carbon while fractional oil of haw kernel is produced, realizes the comprehensive utilization of resource, keeps away
Exempt from only to focus on production single product and ignore the economic value of byproduct.Chinese hawthorn seed is in the rough Chinese hawthorn seed after stifling vaporization
Charcoal maintains original size substantially, can prepare high quality active carbon, but in traditional production process, most hawthorn
Core is only produced a certain specific product using equipment or only focused in pyrolytic process in itself, and enterprise, which lacks, carries out whole thermal decomposition products
The technology and system of Poly-generation comprehensive utilization, lack rough Chinese hawthorn seed charcoal the effective means for preparing activated carbon, can only conduct
Raw material is outer at a low price to be sold to activated carbon factory, has seriously affected the high value added utilization of charcoal.
(2) during product is produced, with not condensable combustible gas and activating reaction gas for being produced in production process etc.
Combustible gas is heating raw material, make use of the calorific value of pyrolysis gas to the utmost, effectively improves the thermal efficiency of system, reduce height
The consumption of grade electric energy, has obvious energy-saving effect.For original whole system, will be produced in Chinese hawthorn seed pyrolytic process
Pyrolysis gas directly empty or burn up, lack the consideration to thermal balance and afterheat utilizing system, not only cause resource and the energy
Significant wastage, and certain pollution is also generated to environment, there is obvious energy-saving and emission-reduction potentiality.
(3) raw material can be made full use of, is disposably produced a variety of suitable for medical and health, food processing and each field of environmental protection
Product.It is different due to fumigating used time production cycle of gasification burner and activation furnace in process of production, can be by an activation furnace
Arrange in pairs or groups multiple stifling gasification burners, same stifling gasification burner can also come out of the stove multiple rough Chinese hawthorn seed charcoal in a production life cycle,
Thus can be by controlling the heating-up temperature of different stifling gasification burners to obtain a variety of oily products, such as control temperature of evaporating 80
Cut in DEG C -108 DEG C can do the raw material of food additives, and the cut in 109 DEG C -169 DEG C can the light industry such as perfume (or spice) processed
The raw material of product, can produce medicinal raw material more than 170 DEG C.
(4) material heating charing, activation are integral, and traditional method charcoal processing and activation process are separated, centres
Needing manually to shift, labor intensity is big, and treatment effeciency is low, and can reduce rough Chinese hawthorn seed charcoal temperature in transportational process,
Need to reheat when activate in next step, cause the waste of the energy.This equipment does not have motion, structure and technique letter
Single, continuous type commercial manufacturing equipment flow is complete, and continuity is strong, reliable, energy conservation and environmental protection.
(5) the stifling gasification burner and activation furnace in this equipment are all conducted heat using external-heat, and furnace gas amount is small, and resistance is low,
Self-produced fuel gases calorific value is high.Combustion product gases do not contact directly as heat carrier with raw material, will not be mixed into charing produce evaporate oil and
In the water-gas that activation section produces, their calorific value is reduced, and gas circulation amount is little inside and outside stove, can reduce air resistance,
Dust-carrying capacity is reduced.
(6) response area of the activation cylinder in this activation furnace is big, can use less mistake with air good mixing
Measure air coefficient, the activated gas requirement being suitably lowered into.Activation furnace body is simple in structure, and consumable quantity is low, and heats passage
Burning velocity and efficiency are higher than grate furnace, and whole furnace body heat-transfer effect is good.
(7) activation process uses physical method, compares pollution of the chemical zinc chloride activation method to environment and the corruption to equipment
Erosion is lower.And chemical zinc chloride activation method easily corrodes since inboard wall of furnace body can be contacted with zinc chloride, produce plate face concavo-convex
Uneven, tilting is even burnt, and causes furnace body service life short, it is necessary to consider the processing of exhaust gas and waste water and equipment in production process
Anticorrosion Problems.
Brief description of the drawings
Fig. 1 is that the extraction of the utility model plant medicinal liquid is integrally tied with a kind of equipment of embodiment of Activated Carbon Production process equipment
Structure schematic diagram.
Embodiment
Specific embodiment of the utility model is given below.Specific embodiment is only used for being further described this practicality newly
Type, does not limit the application scope of the claims.
The utility model provides a kind of plant medicinal liquid extraction and (referring to Fig. 1, is referred to as set with Activated Carbon Production process equipment
It is standby), including activated carbon system of processing, it is characterised in that the equipment further includes fruit stone and fumigates vaporization extraction system and Activated Carbon Production
System；The fruit stone is fumigated vaporization extraction system, activated carbon production system and activated carbon system of processing and is sequentially connected；
The fruit stone, which fumigates vaporization extraction system, includes raw material cabin 1, the first helical feeder 2, stifling gasification burner 3, centre
Storehouse 4, the first condenser 5, the first cooling-water machine 6, first pump 7,8 and first wind turbine 21 of medicine original fluid container；The stove of the stifling gasification burner 3
Body selects carbon steel, and 2 meters high, 1 meter of diameter, material thickness is 10-20mm, and bile duct is located at furnace body center, is that the oil stream that evaporates of evaporation enters
Position, 16 centimetres of bile duct diameter, ventilative pore size on bile duct is less than the size of Chinese hawthorn seed (2-3mm) in order to avoid surrounding mountain
Short, bristly hair or beard core enters bile duct, and the furnace body heat resisting temperature for fumigating gasification burner 3 is higher than 350 DEG C, and assigned temperature is realized under the monitoring of each instrument；
The number amount and type of first condenser 5 are determined according to actual conditions；One end of 1 and first helical feeder 2 of raw material cabin connects
Connect；The other end of first helical feeder 2 is connected with the material inlet of stifling gasification burner 3；The stifling gasification burner 3
Gas entry is connected with extraneous gas pipeline, and the gas entry of coal gas from stifling gasification burner 3 is passed through；The stifling gasification burner
3 discharge port is connected with intermediate bin 4；The evaporation exhanst gas outlet of the stifling gasification burner 3 passes through the cold of pipeline and the first condenser 5
Solidifying tube inlet connection, the heat resisting temperature of the pipeline are higher than 350 DEG C；The condensation-water drain and the first cold water of first condenser 5
Machine 6 connects；First cooling-water machine 6 is connected by the first pump 7 with the condensing water inlet of the first condenser 5；First condensation
The condenser pipe outlet of device 5 is connected by vertical pipeline with medicine original fluid container 8；The condenser pipe outlet VERTICAL TUBE of first condenser 5
The side wall in road is connected by the first wind turbine 21 with the gas returning port of stifling gasification burner 3；
The activated carbon production system include the second helical feeder 9, activation furnace 10, the second wind turbine 22, the 3rd wind turbine 23,
Steam oven 11, the second condenser 12, the second cooling-water machine 13, second pump 14 and secondary medicine stoste fill 15；The stove of the activation furnace 10
Body selects carbon steel, and 2 meters high, 1.4 meters of diameter, the furnace body heat resisting temperature of activation furnace 10 is higher than 1100 DEG C, under the monitoring of each instrument
Realize assigned temperature；The number amount and type of second condenser 12 are depending on actual conditions；The one of second helical feeder 9
End is connected with intermediate bin 4, and the other end is connected with the material inlet of activation furnace 10；The gas entry of the activation furnace 10 and the external world
Gas pipeline connects, and the gas entry of coal gas from activation furnace 10 is passed through；The steam entry of the activation furnace 10 passes through pipe
Road is connected with extraneous oxygen and steam oven 11, and the second wind turbine 22 is provided with pipeline, and the heat resisting temperature of the pipeline is higher than 450 DEG C；
The gas outlet side of the activation furnace 10 is connected by pipeline and activation air valve 24 with the 3rd wind turbine 23, the gas outlet of activation furnace 10
Opposite side is connected by pipeline and evaporation smoke valve 25 with the condensation tube inlet of the second condenser 12, and the heat resisting temperature of the pipeline is high
In 1100 DEG C；3rd wind turbine 23 is connected with the gas returning port of stifling gasification burner 3；The condensation-water drain of second condenser 12
It is connected with the second cooling-water machine 13；Second cooling-water machine 13 is connected by the condensing water inlet of the second pump 14 and the second condenser 12
Connect；The condenser pipe outlet of second condenser 12 is connected by vertical pipeline with secondary medicine original fluid container 15；
The activated carbon system of processing includes cooler 16, pulverizer 17, screening machine 18, type extruder 19 and packaging shaping
Machine 20；The pulverizer 16 is connected with the activated carbon discharge port of activation furnace 10 by pipeline；The cooler 16 and pulverizer 17
Connection；The pulverizer 17 is connected with screening machine 18；The screening machine 18 is connected with type extruder 19；The type extruder 19 with
Packaging forming machine 20 connects.
The utility model plant medicinal liquid is extracted is with the operation principle and workflow of Activated Carbon Production process equipment：
The first step, will be added in raw material cabin 1 by the hawthorn nuclear fuel material for removing sandstone impurity and simple selection processing；Beat
The material inlet of the first helical feeder 2 and stifling gasification burner 3 is opened, by Chinese hawthorn seed feedstock transportation to stifling gasification burner 3, mountain
The volume of short, bristly hair or beard nuclear fuel material accounts for the 1/2-4/5 of the volume of the evaporator in stifling gasification burner 3；Close the first helical feeder 2；
Second step, fruit stone fumigate vaporization extraction system work, and activated carbon production system and activated carbon system of processing are closed；Will
The material inlet of stifling gasification burner 3 is closed, and evaporation exhanst gas outlet is opened；Gas entry is opened, firing up, makes steam stifling
The evaporator temperature changed in stove 3 reaches 90 DEG C -350 DEG C；High temperature pyrolysis gas phase product is by evaporating exhanst gas outlet from stifling vaporization
Discharged in stove 3, the condensation tube inlet of the first condenser 5 is entered by pipeline, the first pump 7, which is opened, makes the first water chiller 6 work；It is high
Product liquid fractional oil of haw kernel stoste and not condensable combustible gas are obtained after warm solution gas-phase product is condensed, fractional oil of haw kernel is former
Liquid is instilled in medicine original fluid container 8 along vertical pipeline, and not condensable combustible gas enters stifling under the action of the first wind turbine 21 along pipeline
The gas returning port of gasification burner 3；Stifling gasification burner 3 can be evenly heated 70-350 minutes, heating time with furnace body size, process raw material
Depending on amount and concrete condition, until vaporization terminates；
3rd step, directly opens the discharge port of stifling gasification burner 3 after vaporization, fumigates the rough mountain in gasification burner 3
After short, bristly hair or beard core charcoal enters intermediate bin 4, without waiting for immediately passing through the second helical feeder 9 and rough Chinese hawthorn seed charcoal be conveyed into activation
In stove 10, the second helical feeder 9 is the batcher that can bear corresponding material temperature；
4th step, activated carbon production system work, fruit stone fumigates vaporization extraction system and activated carbon system of processing is closed；Will
The material inlet of activation furnace 10 is closed, and gas outlet is opened；Gas entry is opened, firing up, make the work in activation furnace 10
Change cylinder temperature and reach 800 DEG C -1100 DEG C, while steam entry is opened, be passed through 300 DEG C -450 DEG C of superheated vapour；Slightly
Chinese hawthorn seed charcoal processed is evenly heated preceding 1/3 period of total time, and evaporation smoke valve 25 is opened, and activation air valve 24 is closed, high temperature
Pyrolysis gas-phase product enters the condensation tube inlet of the second condenser 12 by evaporating 25 place pipeline of smoke valve, and the second pump 14 is opened
The second water chiller 13 is worked, product liquid fractional oil of haw kernel stoste and can not be cold is obtained after high temperature pyrolysis gas phase product is condensed
Solidifying combustible gas, fractional oil of haw kernel stoste are instilled in secondary medicine original fluid container 15 along vertical pipeline, and not condensable combustible gas is in the 3rd wind
Enter the gas returning port of stifling gasification burner 3 under the action of machine 23 along pipeline；When rough Chinese hawthorn seed charcoal is evenly heated rear the 2/3 of total time
Between section, activation air valve 24 is opened, evaporation smoke valve 25 is closed, and high temperature pyrolysis gas phase product is arranged from the gas outlet of activation furnace 10
Go out, enter the gas returning port of stifling gasification burner 3 by activating 24 place pipeline of air valve under the action of the 3rd wind turbine 23；To rough mountain
Short, bristly hair or beard core charcoal be evenly heated total time for 3-10 it is small when, depending on heating time is with furnace body size, the amount of processing raw material and concrete condition, directly
Become loose to material, start to switch to kermesinus, and a large amount of white cigarettes of emerging, activation terminate, and obtain activated carbon；
5th step, the activated carbon discharge port of activation furnace 10 is opened, activated carbon pass sequentially through cooler 16, pulverizer 17,
Screening machine 18, type extruder 19 and packaging forming machine 20, active carbon finished products machine.
Embodiment
The first step, will be added in raw material cabin 1 by the hawthorn nuclear fuel material for removing sandstone impurity and simple selection processing；Beat
The material inlet of the first helical feeder 2 and stifling gasification burner 3 is opened, by Chinese hawthorn seed feedstock transportation to stifling gasification burner 3, mountain
The volume of short, bristly hair or beard nuclear fuel material accounts for the 1/2 of the volume of the evaporator in stifling gasification burner 3；Close the first helical feeder 2；
Second step, fruit stone fumigate vaporization extraction system work, and activated carbon production system and activated carbon system of processing are closed；Will
The material inlet and evaporation exhanst gas outlet of stifling gasification burner 3 are opened；Gas entry is opened, firing up, make stifling vaporization
Evaporator temperature in stove 3 reaches 180 DEG C；High temperature pyrolysis gas phase product is arranged by evaporating exhanst gas outlet from stifling gasification burner 3
Go out, the condensation tube inlet of the first condenser 5 is entered by pipeline, the first pump 7, which is opened, makes the first water chiller 6 work；High temperature pyrolysis
Product liquid fractional oil of haw kernel stoste and not condensable combustible gas are obtained after gas-phase product is condensed, fractional oil of haw kernel stoste edge is perpendicular
Straight pipeline is instilled in medicine original fluid container 8, and not condensable combustible gas enters stifling gasification burner 3 under the action of the first wind turbine 21 along pipeline
Gas returning port；Stifling gasification burner 3 can be evenly heated 240 minutes, heating time is with furnace body size, the amount of processing raw material and specific feelings
Depending on condition, until vaporization terminates；
3rd step, directly opens the discharge port of stifling gasification burner 3 after vaporization, fumigates the rough mountain in gasification burner 3
After short, bristly hair or beard core charcoal enters intermediate bin 4, without waiting for immediately passing through the second helical feeder 9 and rough Chinese hawthorn seed charcoal be conveyed into activation
In stove 10, the second helical feeder 9 is the batcher that can bear corresponding material temperature；
4th step, activated carbon production system work, fruit stone fumigates vaporization extraction system and activated carbon system of processing is closed；Will
The material inlet of activation furnace 10 and gas outlet are opened；Gas entry is opened, firing up, make the activation cylinder in activation furnace 10
Temperature reaches 850 DEG C, while steam entry is opened, and is passed through 300 DEG C of superheated vapour；Flue gas will be evaporated within first 140 minutes
Valve 25 is opened, and activation air valve 24 is closed, and high temperature pyrolysis gas phase product is by evaporating 25 place pipeline of smoke valve into the second condensation
The condensation tube inlet of device 12, the second pump 14, which is opened, makes the second water chiller 13 work, and is obtained after high temperature pyrolysis gas phase product is condensed
Product liquid fractional oil of haw kernel stoste and not condensable combustible gas, fractional oil of haw kernel stoste instill secondary medicine stoste along vertical pipeline
In tank 15, not condensable combustible gas enters the gas returning port of stifling gasification burner 3 under the action of the 3rd wind turbine 23 along pipeline；Afterwards 280
Minute opens activation air valve 24, and evaporation smoke valve 25 is closed, and high temperature pyrolysis gas phase product is discharged from the gas outlet of activation furnace 10,
Enter the gas returning port of stifling gasification burner 3 by activating 24 place pipeline of air valve under the action of the 3rd wind turbine 23；To rough hawthorn
Core charcoal be evenly heated total time for 7 it is small when, depending on heating time is with furnace body size, the amount of processing raw material and concrete condition, until thing
Material becomes loose, starts to switch to kermesinus, and a large amount of white cigarettes of emerging, activation terminate；
5th step, the activated carbon discharge port of activation furnace 10 is opened, activated carbon pass sequentially through cooler 16, pulverizer 17,
Screening machine 18, type extruder 19 and packaging forming machine 20, active carbon finished products machine.
The utility model does not address part and is suitable for the prior art.
Claims (3)
1. a kind of plant medicinal liquid extraction and Activated Carbon Production process equipment, including activated carbon system of processing, it is characterised in that this sets
The standby fruit stone that further includes fumigates vaporization extraction system and activated carbon production system；The fruit stone fumigates vaporization extraction system, activated carbon
Production system and activated carbon system of processing are sequentially connected；
The fruit stone, which fumigates vaporization extraction system, includes raw material cabin, the first helical feeder, stifling gasification burner, intermediate bin, first
Condenser, the first cooling-water machine, the first pump, medicine original fluid container and the first wind turbine；One end of the raw material cabin and the first helical feeder
Connection；The other end of first helical feeder is connected with the material inlet of stifling gasification burner；The stifling gasification burner
Gas entry is connected with extraneous gas pipeline；The discharge port of the stifling gasification burner is connected with intermediate bin；The steam stifling
The evaporation exhanst gas outlet for changing stove is connected by pipeline with the condensation tube inlet of the first condenser；The condensed water of first condenser
Outlet is connected with the first cooling-water machine；First cooling-water machine is connected by the first pump with the condensing water inlet of the first condenser；Institute
The condenser pipe outlet for stating the first condenser is connected by pipeline with medicine original fluid container；The condenser pipe outlet of first condenser is vertical
The side wall of pipeline is connected by the first wind turbine with the gas returning port of stifling gasification burner；
The activated carbon production system includes the second helical feeder, activation furnace, the second wind turbine, the 3rd wind turbine, steam oven, second
Condenser, the second cooling-water machine, the second pump and secondary medicine stoste fill；One end of second helical feeder is connected with intermediate bin,
The material inlet of the other end and activation furnace connects；The gas entry of the activation furnace is connected with extraneous gas pipeline；Institute
The steam entry for stating activation furnace is connected by pipeline with extraneous oxygen and steam oven, and the second wind turbine is provided with pipeline；It is described
The gas outlet side of activation furnace is connected by pipeline and activation air valve with the 3rd wind turbine, and the gas outlet opposite side of activation furnace passes through pipe
Road and evaporation smoke valve are connected with the condensation tube inlet of the second condenser；The gas returning port of 3rd wind turbine and stifling gasification burner connects
Connect；The condensation-water drain of second condenser is connected with the second cooling-water machine；Second cooling-water machine passes through the second pump and second
The condensing water inlet connection of condenser；The condenser pipe outlet of second condenser is connected by vertical pipeline and secondary medicine original fluid container
Connect.
2. plant medicinal liquid extraction according to claim 1 and Activated Carbon Production process equipment, it is characterised in that the activity
Charcoal system of processing includes cooler, pulverizer, screening machine, type extruder and packaging forming machine；The pulverizer and activation furnace
Activated carbon discharge port is connected by pipeline；The cooler is connected with pulverizer；The pulverizer is connected with screening machine；The sieve
Machine is selected to be connected with type extruder；The type extruder is connected with packaging forming machine.
3. plant medicinal liquid extraction according to claim 1 and Activated Carbon Production process equipment, it is characterised in that described stifling
The furnace body of gasification burner and the furnace body of activation furnace select carbon steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721438493.2U CN207227373U (en) | 2017-11-01 | 2017-11-01 | A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721438493.2U CN207227373U (en) | 2017-11-01 | 2017-11-01 | A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207227373U true CN207227373U (en) | 2018-04-13 |
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ID=61850767
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721438493.2U Expired - Fee Related CN207227373U (en) | 2017-11-01 | 2017-11-01 | A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674759A (en) * | 2017-11-01 | 2018-02-09 | 承德本多宝生物科技有限公司 | A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment and technique |
-
2017
- 2017-11-01 CN CN201721438493.2U patent/CN207227373U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674759A (en) * | 2017-11-01 | 2018-02-09 | 承德本多宝生物科技有限公司 | A kind of plant medicinal liquid extraction and Activated Carbon Production process equipment and technique |
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