CN207024284U - A kind of Traditional Chinese medicine decocting equipment - Google Patents
A kind of Traditional Chinese medicine decocting equipment Download PDFInfo
- Publication number
- CN207024284U CN207024284U CN201720143429.5U CN201720143429U CN207024284U CN 207024284 U CN207024284 U CN 207024284U CN 201720143429 U CN201720143429 U CN 201720143429U CN 207024284 U CN207024284 U CN 207024284U
- Authority
- CN
- China
- Prior art keywords
- storage tank
- temporary storage
- decoction
- liquid
- valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
It the utility model is related to a kind of Traditional Chinese medicine decocting equipment, integrate decoction, membrane filtration efficient impurity removal matter, cryogenic film concentration determine decoction accumulate etc. function, by the primary clusterings such as pure water temporary storage tank, Decocting pot, fried liquid temporary storage tank, film filter, target decoction temporary storage tank, membrane concentrator, power controling box, and the composition such as necessary valve, instrument, liquid transmission supercharging device, connecting pipe.
Description
Technical field
It the utility model is related to technical field of medical equipment, and in particular to a kind of Traditional Chinese medicine decocting equipment.
Background technology
Traditional Chinese herbal decoction is one of conventional dosage forms of Chinese medicine, and the quality of decoction quality directly influences clinical efficacy, decoction shadow
It is mainly active ingredient fried in decoction to ring curative effect to material base, therefore to play the clinical efficacy of traditional Chinese herbal decoction, must be most
Active ingredient of the limits ground in fried Chinese medicine.The decoction of Chinese medicine very be particular about, from utensil to the duration and degree of heating, after being decocted first under dosing
On opportunity, the mode etc. added to molten, require that assurance is accurate, and decoct time-consuming, carry, take and also quite have inconvenience.
Ming Dynasty's Li Shizhen exists《Compendium of Materia Medica》Middle proposition：" it is all to take decoction of medicinal ingredients, though product thing is specially smart, the system of repairing such as method, and the person's of boiling medicine crudity is hurried,
Extreme misery is bad, and duration and degree of heating mistake degree, then medicine is also idle.”
Traditional Chinese medicine decocting at present, mainly there is a home-use pannikin of boiling medicine, and the amount of boiling medicine that Hospitals at Present, clinic, pharmacy are conventional
Larger automatic boiling-machine.
The pannikin of boiling medicine of family expenses（Including marmite, buckpot, porcelain pot, there are naked light direct heating type and electric heating type）, family expenses compared with
For convenience.But because general patient and family members lack knowledge of TCM, often to the fried duration and degree of heating, duration, amount of water, now decoct after
It is improper that lower medicinal material addition opportunity etc. is grasped, and makes fried decoction effect often not good enough.
The larger automatic boiling-machine of the conventional amount of boiling medicine of Hospitals at Present, clinic, pharmacy, although automaticity is higher,
It is that, with the development that tcm clinical is applied, these boiling machines still have certain limitation, mainly there is following deficiency
Place：
1）Due to closed decoction, pressure increases during decoction, and high person is up to 10kg/cm2；Temperature also often high water outlet during decoction
100 DEG C of boiling point, high person is up to 150 DEG C.Though high pressure-temperature is advantageous to the dissolution of most of active ingredients, some active ingredients
It may be destroyed in the case of high pressure-temperature.High pressure-temperature also improves some undesired impurities simultaneously（Such as macromolecular fiber, greatly
Molecular polysaccharide, tannin）Dissolution rate.
2）Although high pressure-temperature can kill the pathogenic microbes carried in most of medicinal material, it is possible that it is a small number of not by
Kill, especially mould and some worm's ovums, it is possible to still have minimal residue in decoction, such decoction is for some enteron aisle work(
The weak crowd of energy（Especially infant）Certain health risk is still suffered from, also can be by shadow for the quality guarantee period of decoction storage
Ring.Even if pathogenic microbes are all killed, but the corpse of these pathogenic microbes and its fragment are it is possible to remain in
In decoction, certain influence is still suffered to drug effect.
3）Due to needing to control final amount of liquid medicine, amount of water during decoction is also restrained, so as to it is also possible that effectively into
The stripping quantity divided is restricted, and so as to have influence on curative effect, or needs to increase medicinal material usage amount.
4）Although some automatic boiling-machines are integrated with concentrating function, but this concentration is by simple heating evaporation side
Formula, make moisture evaporation.Although this condensing mode can reduce the water content in decoction, the heating of long period, it is possible to
Some active ingredients are destroyed, and some volatile effective components may also volatilize and lose with steam, so this concentration
Mode is not appropriate for the decoction concentration of volatile effective component.This condensing mode, the moisture of evaporation, which distributes, to be lost, can not
Recycle, cause certain water resource waste.
5）No matter attach or do not attach common concentrating function, existing boiling machine is difficult that final decoction is accurately determined
Volume is collected, to be taken to patient's accurate quantitative analysis.
Utility model content
Conventional boiling machine active ingredient dissolution rate is low, active ingredient destructive rate is high, Wu Fajing to solve for the utility model
Carefully filter, be difficult to concentrate safely and the problems such as accurate quantitative analysis, there is provided a kind of Traditional Chinese medicine decocting equipment, it is by efficiently decocting to fine mistake
Filter efficient concentration to quantify, convenient and efficient.
To solve the problems, such as that prior art is present, the technical solution of the utility model is：A kind of Traditional Chinese medicine decocting equipment, it is special
Sign is：Including water purification water inlet pipe, pure water temporary storage tank, Decocting pot, fried liquid temporary storage tank, film filter, target decoction temporary storage tank,
Membrane concentrator and power controling box；
The described bottom of pure water temporary storage tank and the top of Decocting pot is connected by pipeline；The bottom of Decocting pot and fried liquid
The top of temporary storage tank is connected by pipeline；The top of fried liquid temporary storage tank and the non-permeate outlet end of film filter pass through pipeline
The liquid feeding end of connection, bottom and film filter is connected by pipeline；The permeate outlet end of film filter is kept in target decoction
The top of tank is connected by pipeline；The top of target decoction temporary storage tank and the non-permeate outlet end of membrane concentrator are connected by pipeline
Connect, the liquid feeding end of bottom and membrane concentrator is connected by pipeline；The top of pure water temporary storage tank and the permeate of membrane concentrator go out liquid
End is connected by pipeline.
Described water purification water inlet pipe is connected with pure water temporary storage tank, or is connected with Decocting pot.
Pure water keeps in pot bottom and valve one is provided with the connecting pipe at the top of Decocting pot, decocts pot bottom and fried liquid
Valve two, fried liquid temporary storage tank top and the non-permeate outlet end of film filter are provided with connecting pipe at the top of temporary storage tank
Connecting pipe on be provided with valve four and pressure gauge one, fried liquid keeps in the connecting pipe of pot bottom and film filter liquid feeding end
On be provided with valve three and booster pump one, target decoction keeps in pot bottom with being provided with the connecting pipe of membrane concentrator liquid feeding end
Valve five and booster pump two；With being provided with the connecting pipe of the non-permeate outlet end of membrane concentrator at the top of target decoction temporary storage tank
Valve six and pressure gauge two.
The bottom of described fried liquid temporary storage tank is provided with waste liquid discharge pipe, and valve seven is provided with waste liquid discharge pipe；Or
Person keeps in fried liquid and is provided with waste liquid discharge pipe on connecting pipe of the pot bottom with film filter liquid feeding end.
The bottom of described target decoction temporary storage tank is provided with finished product decoction packing outlet, finished product decoction packing outlet
On be provided with valve eight；Or kept in target decoction and be provided with finished medicines on connecting pipe of the pot bottom with membrane concentrator liquid feeding end
Liquid dispenses outlet.
The bottom of described Decocting pot is provided with ash gate, and periphery is provided with zone of heating.
Described booster pump one and booster pump two is connected by power line with power controling box.
Described film filter is using the micro-filtration or ultrafiltration apparatus of inoranic membrane or organic film, pore size filter 0.0005-15
Micron；Film filter has liquid feeding end, non-permeate outlet end, permeate outlet end.
Described membrane concentrator is using the enrichment facility of NF membrane or reverse osmosis membrane, pore size filter 0.005-5 nanometer；Film
Inspissator has liquid feeding end, non-permeate outlet end, permeate outlet end.
Compared with prior art, it is as follows the advantages of the utility model：
1）The utility model mainly uses semi-enclosed, normal pressure（Or slightly above normal pressure）Decoct, add water to cook temperature and also lead
Control the boiling temperature in water, i.e., 100 DEG C, or even slightly below 100 DEG C.If use other solvents（Such as alcohol type）, temperature
Also the boiling point of solvent is can be controlled in, is decocted relative to high pressure-temperature, the utility model destroys seldom to the active ingredient in medicinal material.
2）The utility model uses membrane filtration pattern, not only can by the pathogenic microbes remained in the decoction decocted out and
Its fragment all filters away, can also be by the useless impurity of a part of macromolecular（Such as macromolecular fiber, macromolecular polysaccharide, divide greatly
Sub- tannin, high molecular weight protein etc.）Filtering is gone out, and decoction is very pure, is substantially increased the security of decoction, also be substantially prolongs
The storage period of decoction.Decoction after membrane filtration pattern filters, pack and deposited more than 180 days under 20 DEG C of environment.
3）The utility model uses efficient cryogenic film condensing mode（It is general to require that concentration process is no more than 40 DEG C）, can be low
Temperature（Normal temperature）The lower moisture by decoction is rapidly filtered out, and this low temperature regime there is no brokenly to the active ingredient in decoction
It is bad, this condensing mode, final medicine liquid volume can relatively accurately be collected according to container scale, it is accurately fixed to patient to be easy to
Amount is taken.
4）The utility model can add a greater amount of water when carrying out medicinal material decoction, so as to increase substantially in medicinal material effectively into
The dissolution rate divided.Substantial amounts of moisture, can be rapidly filtered out, so making by the efficient cryogenic film condensing mode that the utility model uses
A greater amount of water must be added when decocting to be possibly realized.Amount of water when the utility model decocts is relative to existing other kinds of
Boiling machine can increase 2-4 times, and the active ingredient dissolution rate in medicinal material greatly promotes.
5）The water that the utility model film concentrates out, can be recycled, and will not cause to waste.For example concentrated by reverse osmosis membrane
The pure water gone out, it can be directly used for decocting use next time, or for cleaning fried equipment.
Brief description of the drawings
Fig. 1 is the utility model structure diagram；
Fig. 2 is the schematic diagram of the utility model water purification water inlet pipe connected mode two；
Fig. 3 is the schematic diagram of the utility model water purification water inlet pipe connected mode three；
Fig. 4 is the schematic diagram of the utility model waste liquid discharge pipe connected mode two；
Fig. 5 is that the utility model finished product decoction dispenses the schematic diagram of outlet connected mode two；
Fig. 6 is Traditional Chinese medicine decocting process chart of the present utility model.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
The utility model constructs explanation（Referring to Fig. 1）
The utility model includes water purification water inlet pipe 13, pure water temporary storage tank 1, Decocting pot 2, fried liquid temporary storage tank 3, film filter
4th, the primary clustering such as target decoction temporary storage tank 5, membrane concentrator 6 and power controling box 7, and necessary valve, pump, pressure gauge,
Pipe fitting etc..
Film filter 4 is with liquid feeding end 4-1, non-permeate outlet end 4-2, permeate outlet end 4-3.
Membrane concentrator 6 goes out liquid with liquid feeding end 6-1, non-permeate（Concentrate）Hold 6-2, permeate（Pure water）Outlet end 6-
3。
The bottom of pure water temporary storage tank 1 is connected with the top of Decocting pot 2 by pipeline；The bottom of Decocting pot 2 and fried liquid are temporary
The top for depositing tank 3 is connected by pipeline；The top of fried liquid temporary storage tank 3 and the non-permeate outlet end 4-2 of film filter 4 pass through
Pipeline is connected, and bottom is connected with the liquid feeding end 4-1 of film filter 4 by pipeline；The permeate outlet end 4-3 of film filter 4 with
The top of target decoction temporary storage tank 5 is connected by pipeline；The top of target decoction temporary storage tank 5 and the non-permeate of membrane concentrator 6
Outlet end 6-2 is connected by pipeline, and bottom is connected with the liquid feeding end 6-1 of membrane concentrator 6 by pipeline；The top of pure water temporary storage tank 1
Portion is connected with the permeate outlet end 6-3 of membrane concentrator 6 by pipeline.
Water purification water inlet pipe 13 is connected with the top of pure water temporary storage tank 1, or is connected with the top of Decocting pot 2, or temporary with pure water
Deposit the bottom of tank 1, the top of Decocting pot 2 is connected in a manner of three-way pipeline（Referring to Fig. 1, Fig. 2 and Fig. 3）.
Pure water temporary storage tank 1 is with being provided with valve 1, Decocting pot 2 and fried liquid temporary storage tank 3 on the connecting pipe of Decocting pot 2
Connecting pipe on be provided with valve 2 15, the fried top of liquid temporary storage tank 3 is with the non-permeate outlet end 4-2's of film filter 4
Valve 4 17 and pressure gauge 1 are provided with connecting pipe, the fried bottom of liquid temporary storage tank 3 is with the liquid feeding end 4-1's of film filter 4
Valve 3 16 and booster pump 1 or dense with primary filter 9, the bottom of target decoction temporary storage tank 5 and film are provided with connecting pipe
Valve 5 18 and booster pump 2 12 are provided with the liquid feeding end 6-1 of contracting device 6 connecting pipe；The top of target decoction temporary storage tank 5 and film
Valve 6 19 and pressure gauge 2 21 are provided with the non-permeate outlet end 6-2 of inspissator 6 connecting pipe.
Set on the fried bottom of liquid temporary storage tank 3 and the liquid feeding end 4-1 of film filter 4 connecting pipe with threeway connected mode
There is waste liquid discharge pipe 8；Or waste liquid discharge pipe 8 is provided directly with the bottom of fried liquid temporary storage tank 3, and on waste liquid discharge pipe 8
It is provided with valve 7 22（Referring to Fig. 1 and Fig. 4）.
Set on connecting pipe of the bottom of target decoction temporary storage tank 5 with the liquid feeding end 6-1 of membrane concentrator 6 with threeway connected mode
It is equipped with finished product decoction packing outlet 11；Or finished product decoction packing outlet is provided directly with the bottom of target decoction temporary storage tank 5
Pipe 11, and it is provided with valve 8 23 on finished product decoction packing outlet 11（Referring to Fig. 1 and Fig. 5）.
On the fried bottom of liquid temporary storage tank 3 and the liquid feeding end 4-1 of film filter 4 connecting pipe in or settable primary filter
Device 9.
The bottom of Decocting pot 2 is provided with ash gate 2-2, and periphery is provided with zone of heating 2-3.
The zone of heating 2-3 of Decocting pot 2, booster pump 1 and booster pump 2 12 are connected with power controling box 7 respectively by power line
Connect.
The utility model primary clustering explanation
1）Pure water temporary storage tank：For pure water（The pure water that is concentrated out including film and the water purification that the tank is added from water purification water source）
It is temporary.Tank body capacity can be in 10-1000 liters.The pure water that membrane concentrator concentrates out flows into the tank, or adds water purification by filler pipe
To the tank.The current direction Decocting pot kept in the tank.
2）Decocting pot：For the immersion to medicinal material, decoct.Tank body capacity can be in 10-1000 liters（Boiled medicine according to actual commonly use
Amount determines）.The tank carries zone of heating, and mode of heating is electric-heating-wire-heating, or microwave heating, or hot gas heating, or hot liquid
Heating, or the mode such as fuel gas buring heating；Medicinal material is provided with the top of tank body and adds mouth, Chinese medicine can be made to add the tank from this mouthful；
Tank body lower part is provided with ash gate（Waste residue outlet）, the dregs of a decoction after decoction can discharge through the mouth；Ash gate can be opened and closed, and medicinal material is decocted
It is closed mode when boiling, opens ash gate during deslagging.The tank derives from pure water temporary storage tank with water, can also be added by filler pipe net
Water.Medicinal material to be decocted adds the tank, adds water to be soaked, decocted, and decocts well-done decoction and flows to fried liquid temporary storage tank, after decoction
Medicinal material waste residue through bottom ash gate discharge.
3）Fried liquid temporary storage tank：For the temporary of fried liquid and the non-permeate of membrane filtration.Tank body capacity can be in 10-1000
Rise.The temporary liquid source of the tank is in the fried non-permeate of liquid and film filter of Decocting pot.Temporary liquid through primary filter and
Booster pump flows to film filter, and non-permeate returns to the tank after film filter filters.Remaining waste is discharged through waste liquid discharge pipe.
4）Primary filter：The filter used for protection film filter.Using filter cloth or filter paper or filter bag or
The filtering material such as filter screen or filter core, or/and centrifugal filtration device, the decoction to decoct out carry out primary filter, prevented fried
Flow to film filter containing oversized particles in liquid and film filter is quickly blocked.Liquid is through the primary mistake in fried liquid temporary storage tank
Filter, after filtering and then flow to film filter.The primary filter for can arrangement, can select as needed set or do not set
Put.
5）Film filter：For removing larger particles impurity to fried liquid（Such as pathogenic microorganisms and its fragment, macromolecular
Fiber, macromolecular polysaccharide, macro-molecular protein etc.）.For using the micro-filtration or ultrafiltration apparatus of inoranic membrane or organic film, pore size filter
, can be according to the microfiltration membranes or milipore filter in the wanted fried suitable aperture of medicinal material variety selection typically at 0.0005-10 micron.Film mistake
Filter is with liquid feeding end, non-permeate outlet end, permeate outlet end.The supercharging that pressure needed for film filter is close to by front end
The Valve controlling that pump combination rear end is close to reaches.Fried liquid flows into film filter, non-permeate through primary filter and booster pump
Return to fried liquid temporary storage tank, permeate（Remove deimpurity clarification decoction）Flow to target decoction temporary storage tank.
6）Target decoction temporary storage tank：For removing deimpurity clarification decoction through membrane filtration and concentrating through film to remove partial moisture
Concentrated medicament it is temporary.Tank body capacity can be in 10-1000 liters.Decoction in the tank derives from the clarification medicine of film filter outflow
Liquid and the concentrate of membrane concentrator outflow.Decoction in the tank flows to membrane concentrator through booster pump.Concentration through film thickening
Liquid flows into the tank and kept in again.The tank can be with capacity（Liquid volume）Scale is shown, to observe pot liquid volume amount,
After to target medicine liquid volume can stopper film concentration, then through finished product decoction packing outlet outflow dispensed.
7）Membrane concentrator：For being concentrated to the dehydration for removing deimpurity decoction.For nanofiltration or reverse osmosis membrane enrichment facility, mistake
Filter opening footpath is typically at 0.05-5 nanometer.The valve control that the booster pump combination rear end that pressure needed for the device is close to by front end is close to
System reaches.Membrane concentrator is with liquid feeding end, non-permeate（Concentrate）Outlet end, permeate（Pure water）Outlet end.Target decoction
Liquid flows into the inspissator, non-permeate through booster pump in temporary storage tank（Concentrate）Target decoction temporary storage tank, permeate are flowed into again
（Pure water）Flow into pure water temporary storage tank.
8）Power controling box：Power supply and control voltage, electric current, frequency, power etc. are provided to be originally arranged standby electricity component, it is main
Connect the power devices such as booster pump, Decocting pot zone of heating.
9）Booster pump：The liquid being equipped with to make to reach in film filter or in membrane concentrator certain pressure conveys supercharging
Device.To make film filter and membrane concentrator reaches preferable operating efficiency, it is necessary to which lifting fluid concentrates in film filter and film
Pressure in device.Booster pump is needed with the valve regulated discharge matching of film filter and membrane concentrator rear end to reach suitable pressure
By force.
10）Valve：Liquid delivery tube is arranged to turn off or on liquid flowing and reaching certain flow rate
Valve on road, it is easy to control the direction of liquid flowing and flow velocity, predominantly two-way valve, threeway junction optional as needed
With suitable three-way valve, such as valve 2 14（Referring to Fig. 3）, valve 3 16（Referring to Fig. 1）, valve 5 18（Referring to Fig. 1）.
11）Pressure gauge：The pressure gauge that the utility model uses, being can be on connecting pipe, measurable and display tube
The instrument of pressure data in road.
12）Water purification water inlet pipe：For adding the water purification needed for decocting herbs.From meeting the net of food or medicine sanitary standard
Water water source accesses.The pipe may be connected directly at the top of pure water temporary storage tank, or be connected at the top of Decocting pot, or with pure water temporary storage tank bottom
Connected at the top of portion, Decocting pot in a manner of threeway.
13）Waste liquid discharge pipe：Discharge for the waste liquid to being remained after membrane filtration.It is temporary that the pipe can be directly mounted at fried liquid
The bottom of tank is deposited, or is connected to fried liquid in a manner of threeway and keeps in pot bottom to the connecting pipe between film filter liquid feeding end
On.
14）Finished product decoction dispenses outlet：For the outflow of the concentrated medicament formed after being concentrated to film.Target concentrated medicament
Dispensed after pipe outflow.The pipe can be directly mounted at the bottom of target decoction temporary storage tank, or target is connected in a manner of threeway
Decoction is kept on pot bottom to the connecting pipe between membrane concentrator liquid feeding end.
15）Power controling box：For to be powered with electrical component such as booster pump, Decocting pot zone of heating etc. and provide required electricity
Pressure, electric current, FREQUENCY CONTROL etc..Meet Electrical Safety requirement.There is power line with being connected the power controling box and using electrical component.
The part of all contact medicinal materials or decoction is sanitation-grade material in the utility model, such as tank body, the pump housing, pipe
Part, valve body, can use 304 or 316L stainless steels, and seal can use ethylene propylene diene rubber (EPDM) or silica gel or fluorine
Glue etc.；The parts surface finish of contact medicinal material or decoction, bore, angle etc. meet food or medicine sanitation-grade requirement.
Embodiment one（Referring to Fig. 1）：
The present embodiment includes water purification water inlet pipe 13, pure water temporary storage tank 1, Decocting pot 2, fried liquid temporary storage tank 3, primary filter
9th, the primary clustering such as film filter 4, target decoction temporary storage tank 5, membrane concentrator 6 and power controling box 7, and booster pump 1,
Booster pump 2 12, valve 1, valve 2 15, valve 3 16, valve 4 17, valve 5 18, valve 6 19, pressure gauge 1,
Pressure gauge 2 21, waste liquid discharge pipe 8, finished product decoction packing outlet 11 etc..
Film filter 4 is with liquid feeding end 4-1, non-permeate outlet end 4-2, permeate outlet end 4-3.
Membrane concentrator 6 goes out liquid with liquid feeding end 6-1, non-permeate（Concentrate）Hold 6-2, permeate（Pure water）Outlet end 6-
3。
The bottom of Decocting pot 2 is provided with ash gate 2-2, and periphery is provided with zone of heating 2-3.
Water purification water inlet pipe 13 is connected to the top of pure water temporary storage tank 1；The bottom of pure water temporary storage tank 1 and the top of Decocting pot 2
Connected by pipeline；The bottom of Decocting pot 2 is connected with the top of fried liquid temporary storage tank 3 by pipeline；The bottom of fried liquid temporary storage tank 3
Portion is connected with the liquid feeding end 4-1 of film filter 4 by pipeline；Non- permeate outlet end 4-2 and the fried liquid of film filter 4 are kept in
The top of tank 3 is connected by pipeline；The permeate outlet end 4-3 of film filter 4 passes through pipe with the top of target decoction temporary storage tank 5
Road connects；The bottom of target decoction temporary storage tank 5 is connected with the liquid feeding end 6-1 of membrane concentrator 6 by pipeline；Membrane concentrator 6 is not saturating
The top that liquid outlet end 6-2 is crossed with target decoction temporary storage tank 5 is connected by pipeline, the permeate outlet end 6-3 of membrane concentrator 6 with
The top of pure water temporary storage tank 1 is connected by pipeline.
Be provided with valve 1 on the connecting pipe at the top of the bottom of pure water temporary storage tank 1 and Decocting pot 2, the bottom of Decocting pot 2 with
Valve 2 15, the fried bottom of liquid temporary storage tank 3 and the feed liquor of film filter 4 are provided with the connecting pipe at the fried top of liquid temporary storage tank 3
Hold and be disposed with valve 3 16, primary filter 9, booster pump 1,4 non-permeate of film filter on 4-1 connecting pipe
Outlet end 4-2 on the connecting pipe at the fried top of liquid temporary storage tank 3 with being disposed with pressure gauge 1（Close to film filter 4 not
Permeate outlet end 4-2）, valve 4 17, on the bottom of target decoction temporary storage tank 5 and the liquid feeding end 6-1 of membrane concentrator 6 connecting pipe
It is disposed with valve 5 18, booster pump 2 12, the non-permeate outlet end 6-2 of membrane concentrator 6 and the top of target decoction temporary storage tank 5
Connecting pipe on be disposed with pressure gauge 2 21（Close to the non-permeate outlet end 6-2 of membrane concentrator 6）, valve 6 19, give up
Liquid discharge pipe 8 is connected to the connecting pipe upper valve of the fried bottom of liquid temporary storage tank 3 and the liquid feeding end 4-1 of film filter 4 in a manner of threeway
At door 3 16, finished product decoction packing outlet 11 is connected to the bottom of target decoction temporary storage tank 5 and membrane concentrator device 6 in a manner of threeway
On liquid feeding end 6-1 connecting pipe at valve 5 18.
Power controling box 7 is connected with booster pump 1, booster pump 2 12, the zone of heating 2-3 of Decocting pot 2 by power line respectively
Connect.
Each component type selecting selection of the present embodiment is as follows：
Pure water temporary storage tank：Capacity 200L, material are stainless steel 304.
Decocting pot：Capacity 100L, material are stainless steel 304, periphery electrified heating interlayer（Heating medium is conduction oil, added
Thermal power 12Kw）, top tape medicinal material addition mouth, bottom belt ash gate.
Fried liquid temporary storage tank：Capacity 300L, material are stainless steel 304, and band containing mark is shown.
Primary filter：Mono- bag filter/No. 4 filter bags of SGD-B, filter bag material PTFE（Polytetrafluoroethylene (PTFE)）, filtering essence
Spend 5-10 microns, flange-interface DN50.
Film filter：Hydranautics hollow fiber ultrafiltration membrane HUF-160-R, membrane material are sanitation-grade modified PVC, pore size filter
0.01 micron, molecular cut off 100KDa, case material is sanitation-grade UPVC, operating pressure 0.1-0.3MPa.
Target decoction temporary storage tank：Capacity 300L, material are stainless steel 304, and band containing mark is shown.
Membrane concentrator：Hydranautics ultra-low-pressure reverse osmosis film ESPA2-4040, membrane material are sanitation-grade polyamide, pore size filter
0.5 nanometer, case material is stainless steel 304, operating pressure 1-3MPa.
Power controling box：KFC-33006 variable-frequency power sources control cabinets, out-put supply line heat with booster pump, Decocting pot respectively
The connection such as layer.
Booster pump：Booster pump 1 is equipped with for film filter, using Bohai Sea spring BAW-165 sanitary pumps（Pump housing material stainless steel
304, power of motor 4Kw, pass in and out bore 50mm, maximum working pressure (MWP) 0.35MPa）；Booster pump 2 12 is equipped with for membrane concentrator, adopts
With Bohai Sea spring RP8 sanitation-grade impeller pumps（Maximum working pressure (MWP) 1.8MPa, power of motor 5.5Kw, pass in and out bore 50mm, pump housing material
Stainless steel 304）.
Valve：The present embodiment uses sanitary grade ball valve（Valve body is stainless steel 304, and seal is silica gel or polytetrafluoroethyl-ne
Alkene）.Wherein valve 1, valve 2 15, valve 4 17, valve 6 19 are using manually operated sanitary level two-way valve Q41F-25P/R
（DN50/ flanges connect）, valve 3 16, valve 5 18 use manually operated sanitary level tee ball valve Q45F-16C（T-shaped/DN50/ methods
Orchid connection）.Pressure gauge：Pressure gauge 1, pressure gauge 2 21 use Y-100B/ML diaphragms（Main body and diaphragm material
For Stainless steel 316 L flanges connection/pressure range higher limit 4MPa）.
Pipeline：Use sanitation-grade stainless steel pipes（Material is stainless steel 304 or 306L, DN50）.Installation is with being connected：Press
Accompanying drawing 1 is installed and connected, and forms the Traditional Chinese medicine decocting equipment of complete set, in being realized by the technological process of Fig. 6 Traditional Chinese medicine decoctings
Medicine is fried.
It is described above, an embodiment only of the present utility model, it is not intended to limit protection model of the present utility model
Enclose.
Claims (9)
- A kind of 1. Traditional Chinese medicine decocting equipment, it is characterised in that：Including water purification water inlet pipe（13）, pure water temporary storage tank（1）, Decocting pot（2）、 Fried liquid temporary storage tank（3）, film filter（4）, target decoction temporary storage tank（5）, membrane concentrator（6）And power controling box（7）；Described pure water temporary storage tank（1）Bottom and Decocting pot（2）Top connected by pipeline；Decocting pot（2）Bottom with Fried liquid temporary storage tank（3）Top connected by pipeline；Fried liquid temporary storage tank（3）Top and film filter（4）Do not pass through Liquid outlet end（4-2）Connected by pipeline, bottom and film filter（4）Liquid feeding end（4-1）Connected by pipeline；Film filter （4）Permeate outlet end（4-3）With target decoction temporary storage tank（5）Top connected by pipeline；Target decoction temporary storage tank（5） Top and membrane concentrator（6）Non- permeate outlet end（6-2）Connected by pipeline, bottom and membrane concentrator（6）Feed liquor End（6-1）Connected by pipeline；Pure water temporary storage tank（1）Top and membrane concentrator（6）Permeate outlet end（6-3）Pass through pipe Road connects.
- A kind of 2. Traditional Chinese medicine decocting equipment according to claim 1, it is characterised in that：Described water purification water inlet pipe（13）With it is pure Water temporary storage tank（1）Connection, or and Decocting pot（2）Connection.
- A kind of 3. Traditional Chinese medicine decocting equipment according to claim 1 or 2, it is characterised in that：Pure water temporary storage tank（1）Bottom is with decocting Boil tank（2）Valve one is provided with the connecting pipe at top（14）, Decocting pot（2）Bottom and fried liquid temporary storage tank（3）Top Valve two is provided with connecting pipe（15）, fried liquid temporary storage tank（3）Top and film filter（4）Non- permeate outlet end （4-2）Connecting pipe on be provided with valve four（17）With pressure gauge one（20）, fried liquid temporary storage tank（3）Bottom and film filter （4）Liquid feeding end（4-1）Connecting pipe on be provided with valve three（16）With booster pump one（10）, target decoction temporary storage tank（5）Bottom Portion and membrane concentrator（6）Liquid feeding end（6-1）Connecting pipe on be provided with valve five（18）With booster pump two（12）；Target decoction Temporary storage tank（5）Top and membrane concentrator（6）Non- permeate outlet end（6-2）Connecting pipe on be provided with valve six（19）And pressure Power table two（21）.
- A kind of 4. Traditional Chinese medicine decocting equipment according to claim 3, it is characterised in that：Described fried liquid temporary storage tank（3）'s Bottom is provided with waste liquid discharge pipe（8）, waste liquid discharge pipe（8）On be provided with valve seven（22）；Or in fried liquid temporary storage tank（3） Bottom and film filter（4）Liquid feeding end（4-1）Connecting pipe on be provided with waste liquid discharge pipe（8）.
- A kind of 5. Traditional Chinese medicine decocting equipment according to claim 4, it is characterised in that：Described target decoction temporary storage tank（5） Bottom be provided with finished product decoction packing outlet（11）, finished product decoction packing outlet（11）On be provided with valve eight（23）； Or in target decoction temporary storage tank（5）Bottom and membrane concentrator（6）Liquid feeding end（6-1）Connecting pipe on be provided with finished product decoction point Fill outlet（11）.
- A kind of 6. Traditional Chinese medicine decocting equipment according to claim 5, it is characterised in that：Described Decocting pot（2）Bottom set It is equipped with ash gate（2-2）, periphery is provided with zone of heating（2-3）.
- A kind of 7. Traditional Chinese medicine decocting equipment according to claim 6, it is characterised in that：Described booster pump one（10）And supercharging Pump two（12）Pass through power line and power controling box（7）Connection.
- A kind of 8. Traditional Chinese medicine decocting equipment according to claim 7, it is characterised in that：Described film filter（4）To use The micro-filtration or ultrafiltration apparatus of inoranic membrane or organic film, pore size filter 0.0005-15 microns；Film filter（4）With liquid feeding end（4- 1）, non-permeate outlet end（4-2）, permeate outlet end（4-3）.
- A kind of 9. Traditional Chinese medicine decocting equipment according to claim 8, it is characterised in that：Described membrane concentrator（6）To use The enrichment facility of NF membrane or reverse osmosis membrane, pore size filter 0.005-5 nanometers；Membrane concentrator（6）With liquid feeding end（6-1）, not Permeate outlet end（6-2）, permeate outlet end（6-3）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720143429.5U CN207024284U (en) | 2017-02-17 | 2017-02-17 | A kind of Traditional Chinese medicine decocting equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720143429.5U CN207024284U (en) | 2017-02-17 | 2017-02-17 | A kind of Traditional Chinese medicine decocting equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207024284U true CN207024284U (en) | 2018-02-23 |
Family
ID=61472259
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720143429.5U Active CN207024284U (en) | 2017-02-17 | 2017-02-17 | A kind of Traditional Chinese medicine decocting equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207024284U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110251398A (en) * | 2019-07-19 | 2019-09-20 | 扬州罗素生物技术有限公司 | A kind of purification granulation device of Chinese medicine |
-
2017
- 2017-02-17 CN CN201720143429.5U patent/CN207024284U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110251398A (en) * | 2019-07-19 | 2019-09-20 | 扬州罗素生物技术有限公司 | A kind of purification granulation device of Chinese medicine |
| CN110251398B (en) * | 2019-07-19 | 2023-07-07 | 扬州罗素生物技术有限公司 | Purification pelletization device of traditional chinese medicine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101530674B (en) | Unit-combination type extracts technique and the device of Effective Component of Chinese Medicine | |
| CN101843930B (en) | Household automated peritoneal dialysis device | |
| CN106904782A (en) | Drinking pure closed cycle supply system and its control method | |
| CN201710718U (en) | Simple and convenient automatic peritoneal dialysis equipment | |
| CN101862481A (en) | Simple automatic peritoneal dialysis equipment | |
| CN207024284U (en) | A kind of Traditional Chinese medicine decocting equipment | |
| CN207047040U (en) | Drinking pure closed cycle supply system | |
| CN201871012U (en) | Solution supply and dispensing system of hemodialysis machine | |
| CN110078279A (en) | A kind of processing technology of selenium-rich water | |
| CN206482898U (en) | A kind of hemodialysis system | |
| CN205241379U (en) | Concentrated water recycle's purifier | |
| CN209052528U (en) | A kind of drinking water disinfection separating barrel | |
| CN206868040U (en) | A kind of complete liquid mixing system of liquid drugs injection | |
| CN208151133U (en) | A kind of direct drinking water system | |
| CN206447741U (en) | A kind of Treated sewage reusing processing equipment | |
| CN106927518A (en) | A kind of desk-top water purifier with humidification function | |
| CN204723407U (en) | A kind of Chinese medicine extraction thickener | |
| CN207108520U (en) | A kind of desk-top water purifier with humidification function | |
| CN205528109U (en) | Chemical industry workshop pure water preparation system | |
| CN207891150U (en) | A kind of plateau mountain area high service water cleaning systems | |
| TW201806877A (en) | High-magnesium-content concentrate, and mixing system of high-magnesium-content drinking water capable of mixing high-magnesium-content concentrate and purified water to obtain a high-magnesium-content drinking water which provides significant positive influences on human body | |
| CN206751582U (en) | A kind of direct drinking fountain of waste water reusable edible | |
| CN2596985Y (en) | Medicinal liquid preparation device | |
| CN206680223U (en) | Multistage purification of water system | |
| CN205760134U (en) | A kind of filtering drinking water device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |