CN107158729A - Concentration systems and alcohol precipitation concentration systems - Google Patents
Concentration systems and alcohol precipitation concentration systems Download PDFInfo
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- CN107158729A CN107158729A CN201710545567.0A CN201710545567A CN107158729A CN 107158729 A CN107158729 A CN 107158729A CN 201710545567 A CN201710545567 A CN 201710545567A CN 107158729 A CN107158729 A CN 107158729A
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- heater
- concentration systems
- accommodating chamber
- steam
- heating tube
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 9
- 238000001556 precipitation Methods 0.000 title claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 74
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000003756 stirring Methods 0.000 claims description 18
- 238000005374 membrane filtration Methods 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 8
- 230000005494 condensation Effects 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 3
- 238000002955 isolation Methods 0.000 claims 2
- 230000037237 body shape Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 20
- 239000003814 drug Substances 0.000 description 33
- 239000002994 raw material Substances 0.000 description 32
- 239000012141 concentrate Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 239000006229 carbon black Substances 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 6
- 238000013019 agitation Methods 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000012266 salt solution Substances 0.000 description 4
- 239000004480 active ingredient Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- 230000008719 thickening Effects 0.000 description 3
- 230000000875 corresponding effect Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000001595 contractor effect Effects 0.000 description 1
- 230000004069 differentiation Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
- B01D61/366—Apparatus therefor
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
- C09C1/48—Carbon black
- C09C1/56—Treatment of carbon black ; Purification
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention relates to concentrator field, in particular to a kind of concentration systems and alcohol precipitation concentration systems.The concentration systems include heater, moisture separation device and condensing unit.Heater is connected with moisture separation device by vapour pipe group, and moisture separation device is connected with condensing unit by escape pipe.Heater includes isolating device and heater body.Isolating device is arranged in heater body and is flexibly connected with heater body.First accommodating chamber and the second accommodating chamber are set in heater body；First accommodating chamber and the second accommodating chamber are respectively, optionally located at the relative both sides of isolating device.It can be isolated the isolated liquid of enrichment materials liquid and moisture separation device, accelerated the speed of concentration, saved the production time, improve production efficiency.
Description
Technical field
The present invention relates to concentrator field, in particular to a kind of concentration systems and alcohol precipitation concentration systems.
Background technology
In the preparation process of liquid preparation, the concentration of liquid is often referred to, concentration is to remove the moisture in material liquid,
With the concentration and content of the active ingredient needed for increase in the solution, then to strengthen corresponding effect of liquid preparation.
Existing condensing mode uses steam condensation concentration, not good using which concentrated effect, dense in order to improve
Contracting effect, constantly concentrate is repeatedly circulated in actual production, but which improvement is not good, while also add production
Cost and generation time.And corresponding steam condensation enrichment facility is also to mix enrichment materials liquid and circulation concentrate, increase
Production cost and time.Meanwhile, existing steam condenses enrichment facility, and the rate of heat addition is slow, adds the waste of energy.
The content of the invention
It is an object of the invention to provide a kind of concentration systems, it can separate enrichment materials liquid and moisture separation device
Obtained liquid is isolated, and is accelerated the speed of concentration, has been saved the production time, improves production efficiency.
, can be significantly by the production system another object of the present invention is to provide a kind of alcohol precipitation concentration production system
Reduction energy consumption, economize on resources, so save production cost.
What embodiments of the invention were realized in：
A kind of concentration systems, it includes the steam separation of the heater, separation water vapour and decoction for heating decoction
The condensing unit of device and condensed steam.Heater is connected with moisture separation device by vapour pipe group, steam separation
Device is connected with condensing unit by escape pipe.Heater includes isolating device and heater body.Isolating device is set
It is flexibly connected in heater body and with heater body.It is provided with heater body and accommodates the of enrichment materials
One accommodating chamber and the second accommodating chamber for accommodating the isolated solution of moisture separation device；First accommodating chamber and the second accommodating chamber difference
It may be selectively provided in the relative both sides of isolating device.
In preferred embodiments of the present invention, above-mentioned heater also includes membrane filtration device.Membrane filtration device
Discharging opening is connected with the charging aperture of heater body.
In preferred embodiments of the present invention, above-mentioned heater includes the first heating tube.First heating tube is held along first
Receive chamber circumferential annular disk located at heater sheet it is external.
In preferred embodiments of the present invention, above-mentioned heater also includes agitating device.Agitating device is optionally
It is arranged in the first accommodating chamber, and one end of agitating device is connected with heater body.
In preferred embodiments of the present invention, above-mentioned agitating device includes agitating shaft, multiple stirring parts and multiple ultrasonic waves
Generator.One end of agitating shaft sets device body with heating and is connected, and multiple stirring parts are sheathed on outside agitating shaft, multiple ultrasonic waves
Generator is positioned in agitating shaft and multiple stirring parts.
In preferred embodiments of the present invention, above-mentioned heater includes the second heating tube.Second heating tube, which is arranged on, to be added
In thermal body, and the second heating tube is optionally arranged at the second accommodating chamber around the circumferential annular of heater body
It is interior.
In preferred embodiments of the present invention, above-mentioned vapour pipe group includes air inlet pipe and drain pipe.Heater goes out vapour
Mouthful be connected with one end of air inlet pipe, the air intake connection of the other end and moisture separation device of air inlet pipe, one end of drain pipe and
Second accommodating chamber is connected, and the other end of drain pipe and the liquid outlet of moisture separation device are connected.
In preferred embodiments of the present invention, above-mentioned isolating device includes the 3rd heating tube and isolating device body, the 3rd
Heating tube is arranged in isolating device body.
In preferred embodiments of the present invention, above-mentioned moisture separation device includes moisture separation device body, steam and separated
Axle and steam separation member, steam separation axle and steam separation member be respectively provided with moisture separation device body, steam separation axle
One end is connected with moisture separation device body, and steam separation member is sheathed on outside steam separation axle, and is separated with steam axle and slided company
Connect.
A kind of alcohol precipitation concentration systems, it includes above-mentioned concentration systems.
The beneficial effect of the embodiment of the present invention is：The concentration systems of the present invention make it by the way that carbon black is repeatedly transported
Temperature fall, saves energy consumption, lifts the efficiency of concentration systems.Carbon black is repeatedly screened and removed by multiple screening installations
It is miscellaneous, the quality of carbon black is lifted, and the carbon black of different size is packed using wrapper, enhance the production capacity of concentration systems.Bag
Carbon black production system containing the concentration systems, production carbon black that can be fast and automatically, while saving the production time and being produced into
This.
Brief description of the drawings
In order to illustrate the technical solution of the embodiments of the present invention more clearly, below will be attached to what is used required in embodiment
Figure is briefly described, it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, therefore is not construed as pair
The restriction of scope, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to this
A little accompanying drawings obtain other related accompanying drawings.
Fig. 1 is the structural representation for the concentration systems that the embodiment of the present invention 1 is provided；
Fig. 2 is the structural representation for the heater that the embodiment of the present invention 1 is provided；
Fig. 3 is the structural representation for the 3rd heating tube that the embodiment of the present invention 1 is provided；
Fig. 4 is the structural representation for the agitating device that the embodiment of the present invention 1 is provided.
Icon：100- concentration systems；110- heaters；120- moisture separation devices；130- condensing units；140- steam
Pipe group；150- membrane filtration devices；111- heater bodies；160- isolating devices；The accommodating chambers of 113- first；115- second holds
Receive chamber；The heating tubes of 117- first；The heating tubes of 119- second；170- agitating devices；171- agitating shafts；173- stirring parts；175- surpasses
Sonic generator；180- concentrate liquid outlets；121- moisture separation device bodies；123- steam separates axle；125- steam is separated
Part；127- zones of heating；141- air inlet pipe；143- drain pipes；131- condensers；133- coolers；135- submerged soils；132- is condensed
Device body；134- condenser pipes；136- cooler bodies；138- cooling tubes；The heating tubes of 161- the 3rd；163- isolating device bodies.
Embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below in conjunction with the embodiment of the present invention
In accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
A part of embodiment of the present invention, rather than whole embodiments.The present invention implementation being generally described and illustrated herein in the accompanying drawings
The component of example can be arranged and designed with a variety of configurations.
Therefore, the detailed description of embodiments of the invention below to providing in the accompanying drawings is not intended to limit claimed
The scope of the present invention, but be merely representative of the present invention selected embodiment.Based on the embodiment in the present invention, this area is common
The every other embodiment that technical staff is obtained under the premise of creative work is not made, belongs to the model that the present invention is protected
Enclose.
It should be noted that：Similar label and letter represents similar terms in following accompanying drawing, therefore, once a certain Xiang Yi
It is defined in individual accompanying drawing, then it further need not be defined and explained in subsequent accompanying drawing.
In the description of the invention, it is necessary to which explanation, term " first ", " second ", " the 3rd " etc. are only used for differentiation and retouched
State, and it is not intended that indicating or implying relative importance.
In the description of the invention, in addition it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ",
" connection ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or one
Connect body；Can be mechanical connection or electrical connection；Can be joined directly together, can also be indirect by intermediary
It is connected, can is the connection of two element internals.For the ordinary skill in the art, on being understood with concrete condition
State the concrete meaning of term in the present invention.
Below in conjunction with the accompanying drawings, some embodiments of the present invention are elaborated.It is following in the case where not conflicting
Feature in embodiment and embodiment can be mutually combined.
Embodiment 1
As shown in figure 1, the present embodiment provides a kind of concentration systems 100, it includes the heater for being used to heat decoction
110th, the condensing unit 130 of the moisture separation device 120 and the condensation vapor of separation water vapour and decoction；The heating
Device 110 is connected with the moisture separation device 120 by vapour pipe group 140, the moisture separation device 120 and the condensation
Device 130 is connected by escape pipe.
Heater 110 includes heater body 111 and membrane filtration device 150, the discharging of membrane filtration device 150
Mouth is connected with the charging aperture of the heater body 111.And membrane filtration device 150 is arranged on heater body 111
Side.The solid impurity in decoction can be separated before heating condensation concentration is carried out using membrane filtration device 150,
Ensure in the decoction concentrated only containing moisture and required active ingredient, it is ensured that the efficiency of concentration, reduce after concentration
Reprocessing.
Further, with reference to Fig. 1 and Fig. 2, heater 110 also includes isolating device 160, and isolating device 160 is arranged on
It is flexibly connected in heater body 111 and with heater body 111.Isolating device 160 can by concentrated medicament raw material with
The solution obtained by moisture separation device 120 i.e. the first liquid is isolated, and prevents the two from mixing again, reduces time of concentration
Several quantity, while ensureing the effect of concentration.When concentration systems 100 are concentrated, isolating device 160 and heater body
111 are fixedly connected, and the favorable sealing property between isolating device 160 and heater body 111, can prevent concentrated medicament
Raw material flows through isolating device 160 and the gap in heater body 111, and isolating device 160 will not be subjected to displacement.Work as concentration
After the completion of system 100 is concentrated, rotation isolating device 160 enables the liquid in isolating device 160 smoothly to flow down.Need explanation
, the annexation of isolating device 160 and heater body 111 can be nuts and bolt be connected or
Latch connection is either hinged.Further, the shape of the cross section of isolating device 160 and heater body 111 is transversal
The shape in face is consistent, it is ensured that isolating device 160 can be acted on well with heater body 111.
Further, the first accommodating chamber 113 for accommodating enrichment materials is provided with heater body 111 and steam is accommodated
The isolated solution of separator 120 is the second accommodating chamber 115 of the first liquid；First accommodating chamber 113 and the second accommodating chamber 115
It is alternative respectively to be located at the relative both sides of isolating device 160.Isolating device 160 is being used to concentrated medicament raw material and first
When liquid is isolated, the inside isolated device 160 of heater body 111 is isolated into two spaces i.e. the first accommodating chamber
113 and second accommodating chamber 115.And after the completion of concentration, rotating isolating device 160 so that the first accommodating chamber 113 and second is accommodated
Chamber 115 is connected, and now the inner liquid medicine of the first accommodating chamber 113 is flowed in the second accommodating chamber 115, and with the second accommodating chamber 115
First liquid is mixed, and the two second liquid being mixed to get is the decoction that concentration completes to obtain.
Further, referring to Fig. 3, isolating device 160 includes the 3rd heating tube 161 and isolating device body 163, and the 3rd adds
Heat pipe 161 is arranged in isolating device body 163.When concentration systems 100 are concentrated, the 3rd heating tube 161 be arranged on every
The concentrated medicament raw material in first accommodating chamber 113 is further heated from the interior energy of device body 163, accelerates concentration speed,
Shorten the production time.Meanwhile, the 3rd heating tube 161 can also be incubated to the first liquid in the second accommodating chamber 115, it is to avoid
First fluid temperature is reduced, and when carrying out subsequent operation, is also needed again to heat it, is further reduced energy consumption.
Further, the disk of the 3rd heating tube 161 is located in isolating device body 163, can be increased by the way of disk is set
The contact area of concentrated medicament raw material and the first liquid and heating tube, and then the rate of heat addition and efficiency are lifted, further increase
The efficiency of concentration.Further, isolating device body 163 uses inside for hollow structure, and isolating device body 163 is using empty
Core structure can reduce the amount of the heat and heat exchange with outside of the 3rd heating tube 161 generation, the heat that the 3rd heating tube 161 of protection is produced
It can be swapped as much as possible with concentrated medicament raw material and the first liquid, further, reduce energy loss, lifting concentration
Efficiency.
Further, heater 110 includes the first heating tube 117.First heating tube 117 is along the first accommodating chamber 113
Circumferential annular disk is outside heater body 111.When concentration systems 100 are concentrated, the first 117 pair first of heating tube is held
The concentrated medicament raw material of chamber 113 received is heated so that concentrated medicament raw material can quickly be heated and be concentrated.First adds
Can be that the vapor with higher-energy can also be the resistive heater that can quickly heat in heat pipe 117.First heating tube
117 by the way of disk is set, by increasing capacitance it is possible to increase its efficiency of heating surface, accelerates the speed of concentrated medicament raw material concentration, shortens the production time,
Simultaneously, it is ensured that during concentration, concentrated medicament raw material each several part is heated evenly, it is ensured that active ingredient in concentrated medicament raw material will not be because
Activity is reduced to be too high or too low for temperature.
Further, heater 110 includes the second heating tube 119.Second heating tube 119 is arranged on heater body
In 111, and the second heating tube 119 is optionally arranged at the second accommodating chamber 115 around the circumferential annular of heater body 111
It is interior.When concentration systems 100 are concentrated, the second heating tube 119 can be protected to the first liquid in the second accommodating chamber 115
Temperature, and during the stopping concentration of concentration systems 100, the second heating tube 119 can also be entered to the second liquid in heater body 111
Row insulation, it is ensured that thickening efficiency.
Further, heater 110 also includes agitating device 170.Agitating device 170 is optionally arranged at first
In accommodating chamber 113, and one end of agitating device 170 is connected with heater body 111.Agitating device 170 is used to mix
Concentrated medicament raw material, it is ensured that concentrated medicament raw material each several part is heated evenly, meanwhile, it is capable to the water more conducively in concentrated medicament raw material
Evaporated, thickening efficiency can be lifted, accelerate concentration speed.
Further, referring to Fig. 4, agitating device 170 includes agitating shaft 171, multiple stirring parts 173 and multiple ultrasonic waves hair
Raw device 175.One end of agitating shaft 171 sets device body with heating and is connected, and multiple stirring parts 173 are sheathed on outside agitating shaft 171,
Multiple supersonic generators 175 are positioned in agitating shaft 171 and multiple stirring parts 173.One end of agitating shaft 171 and turning for motor
Axle is connected, and drives agitating shaft 171 to rotate when machine shaft is rotated, and then drives stirring parts 173 to move, to realize to concentrated medicament
The stirring of raw material.And motor is placed on the top of heater body 111.Stirring parts 173 are spiral helicine stirring structure, using spiral shell
The stirring parts of rotation shape, which are stirred, can increase the contact area of liquid and stirring parts 173, be more conducive to liquid agitation is uniform.Together
When, ultrasonic wave can be produced using supersonic generator 175, further promote stirring for enrichment materials decoction, lifted dense
The effect of contracting.Supersonic generator 175 is both provided with agitating shaft 171 and stirring parts 173, by increasing capacitance it is possible to increase the ultrasonic wave of generation
Quantity, further promote the effect being uniformly mixed.
Further, heater 110 also includes concentrate liquid outlet 180, and concentrate liquid outlet 180 is arranged on heating dress
Put the bottom of body 111.After concentration systems 100 complete to concentrate and rotate division board, the liquid and second in the first accommodating chamber 113
The first liquid in accommodating chamber 115 is mixed to get after second liquid, concentrate liquid outlet 180 is opened, by the liquid being concentrated to give
Stored, be easy to subsequent operation.
Further, moisture separation device 120 includes moisture separation device body 121, steam separation axle 123 and steam point
Off member 125, steam separation axle 123 and steam separation member 125 be respectively provided with moisture separation device body 121, steam separation axle
123 one end is connected with moisture separation device body 121, and steam separation member 125 is sheathed on outside steam separation axle 123, and and water
Vapour separation axle 123 is slidably connected.When concentration systems 100 are operated, concentrated medicament raw material is heated by heater 110, is entered
And become vapor, but contain the drop of fraction of concentrated medicament raw material in the vapor, if not to the decoction in vapor
Drop is reclaimed, and adds production cost, reduces yield.Accordingly, it would be desirable to which vapor and decoction drop are separated.Water
When steam and decoction drop are by moisture separation device 120, vapor acts on steam separation member 125, promotes steam separation member
125 are moved upwards along steam separation axle 123, and now, the condensing unit 130 that vapor continues to move to rear end is condensed, and
Decoction drop is then stopped by steam separation member 125, prevents its condensing unit 130 for continuing rear end from moving, then realizes water
The separation of steam and decoction drop.
Vapor is that steam separation member 125 can produce heat exchange, vapor easy regelation when contact
For water, and then thickening efficiency is reduced, therefore, in order to reduce the possibility and quantity that vapor is re-condensed into aqueous water,
One layer of zone of heating 127 is wrapped outside moisture separation device body 121, it is heated so that vapor and decoction drop have
Energy will not have greatly changed.
Further, vapour pipe group 140 includes air inlet pipe 141 and drain pipe 143.The venthole of heater 110 is with entering
One end connection of tracheae 141, the other end of air inlet pipe 141 is connected with the air intake of moisture separation device 120, drain pipe 143
One end is connected with the second accommodating chamber 115, and the other end of drain pipe 143 is connected with the liquid outlet of moisture separation device 120.Air inlet pipe
141 be used for by heated in heater to vapor be passed in moisture separation device 120, and drain pipe 143 is used for water
The isolated decoction drop of steum separating device 120 is recovered in the second accommodating chamber 115 of heater 110.
Further, condensing unit 130 includes condenser 131, cooler 133 and the submerged soil 135 being sequentially connected, condensation
Device 131 is connected with moisture separation device 120.Condensed after entering condenser 131 by the vapor of moisture separation device 120
Aqueous water is obtained, it is that it has higher thermal energy that now the temperature of aqueous water is still higher, is then cooled down, is cooled to one
Stored after constant temperature degree in submerged soil 135, be easy to subsequent dilution alcohol or operation.
Specifically, condenser 131 includes condenser body 132 and condenser pipe 134, and condenser pipe 134 is arranged on condenser sheet
In body 132, and set along the circumferential annular of condenser body 132, the salt solution of reduction temperature is provided with condenser pipe 134, is used
Salt solution quickly can carry out heat exchange with vapor, accelerate the condensation of vapor.
Specifically, cooler 133 includes cooler body 136 and cooling tube 138, and cooling tube 138 is arranged on cooler sheet
In body 136, and set along the circumferential annular of cooler body 136, the salt solution of reduction temperature is provided with cooling tube 138, is used
Salt solution can quickly carry out heat exchange, the cooling of acceleration hot water with the water of higher temperature.
In the present embodiment, the operating method and principle of concentration systems：
When concentration systems are concentrated, isolating device is fixedly connected with heater body, by heater body
Portion is isolated into the first accommodating chamber and the second accommodating chamber, and concentrated medicament raw material is placed in the first accommodating chamber, then opens first
Heating tube and the 3rd heating tube 161 are heated to concentrated medicament raw material.Meanwhile, open agitating device and concentrated medicament raw material is entered
Row mechanical agitation and ultrasonic agitation, are constantly raised, the water in concentrated medicament raw material is changed into water with the temperature of concentrated medicament raw material
Steam is evaporated out of concentrated medicament raw material, and moves in moisture separation device, and vapor promotes steam separation member along water
Move upwards in the direction of vapour separation axle.Now, the drop of the concentrated medicament raw material of entrainment is stopped by steam separation member in vapor
Condensing unit can not be entered, and drop into the bottom of moisture separation device, then flow in the second accommodating chamber of heater
Stored.Vapor is easy to follow-up profit by being condensed, being cooled down and being stored into condensing unit after moisture separation device
The operation such as alcohol dilution is carried out with the water.
Implement 2
The basic structure phase for the concentration systems that the basic structure for the concentration systems that the present embodiment is provided is provided with embodiment 1
Seemingly, difference is that the concentration systems of the present embodiment do not contain condensing unit.
By heating concentrated medicament raw material so that the moisture in it is changed into gaseous vapor is steamed out of concentrated medicament raw material
Issue, to realize the concentration of heating concentrated medicament raw material, but the vapor of part evaporation has higher energy, if directly
Connect and condensed and cooled down, waste its high heat energy having, therefore, in order to save energy consumption, reduce production cost, can be straight
Connect and above-mentioned with having high heat energy vapor is passed through in the first heating tube or the second heating tube to concentrated medicament raw material or the
One liquid carries out heating and thermal insulation, then reclaims the less vapor of heat energy and carries out later use again.Using aforesaid way
Number of devices can be reduced, production cost is reduced, meanwhile, it is capable to which energy consumption needed for reducing heating, further reduces production cost, together
When shorten the heat time.
In summary, the present invention is by the way that concentrated medicament raw material and the isolated liquid of moisture separation device are deposited respectively
Put, improve concentrated effect, prevent from heating concentrated medicament raw material repeatedly, reduce energy consumption.Meanwhile, using mechanical agitation and
Ultrasonic agitation is combined, and increases the equal degree of mixing of concentrated medicament raw material, it is ensured that concentrated medicament raw material each several part is heated evenly, lifting
The concentrated effect of concentration systems.
Upper described only the preferred embodiments of the present invention, are not intended to limit the invention, for the technology of this area
For personnel, the present invention can have various modifications and variations.Within the spirit and principles of the invention, that is made any repaiies
Change, equivalent substitution, improvement etc., should be included in the scope of the protection.
Claims (10)
1. a kind of concentration systems, it is characterised in that include the water of the heater for heating decoction, separation water vapour and decoction
The condensing unit of steum separating device and the condensation water vapour；The heater passes through steam with the moisture separation device
Pipe group is connected, and the moisture separation device is connected with the condensing unit by escape pipe；The heater includes isolation and filled
Put and be arranged on heater body, the isolating device in the heater body and movable with the heater body
Connection；The first accommodating chamber for accommodating enrichment materials is provided with the heater body and the moisture separation device point is accommodated
From the second accommodating chamber for obtaining solution；First accommodating chamber and second accommodating chamber respectively, optionally located at it is described every
The both sides relative from device.
2. concentration systems according to claim 1, it is characterised in that the heater also includes membrane filtration device,
The discharging opening of the membrane filtration device is connected with the charging aperture of the heater body.
3. concentration systems according to claim 2, it is characterised in that the heater includes the first heating tube, described
Circumferential annular disk of first heating tube along first accommodating chamber is external located at the heater sheet.
4. concentration systems according to claim 3, it is characterised in that the heater also includes agitating device, described
Agitating device is optionally arranged in first accommodating chamber, and one end of the agitating device and the heater sheet
Body is connected.
5. concentration systems according to claim 4, it is characterised in that the agitating device includes agitating shaft, multiple stirrings
Part and multiple supersonic generators, one end of the agitating shaft are connected with the heater body, and multiple stirring parts are equal
It is sheathed on outside the agitating shaft, multiple supersonic generators are positioned in the agitating shaft and multiple stirring parts.
6. concentration systems according to claim 1, it is characterised in that the heater includes the second heating tube, described
Second heating tube is arranged in the heater body, and second heating tube is around the circumferential ring of the heater body
Shape is optionally arranged in second accommodating chamber.
7. concentration systems according to claim 1, it is characterised in that the vapour pipe group includes air inlet pipe and drain pipe,
The venthole of the heater is connected with one end of the air inlet pipe, and the other end of the air inlet pipe separates dress with the steam
The air intake connection put, one end of the drain pipe connects with second accommodating chamber, the other end of the drain pipe with it is described
The liquid outlet connection of moisture separation device.
8. concentration systems according to claim 1, it is characterised in that the isolating device includes the 3rd heating tube and isolation
Device body, the 3rd heating tube is arranged in the isolating device body.
9. concentration systems according to claim 8, it is characterised in that the moisture separation device includes moisture separation device
Body, steam separation axle and steam separation member, the steam separation axle and the steam separation member are respectively provided with and the steam point
From in device body, one end of the steam separation axle is connected with the moisture separation device body, the steam separation member set
Separated located at the steam outside axle, and axle is separated with the steam and be slidably connected.
10. a kind of alcohol precipitation concentration systems, it is characterised in that including the concentration systems as described in claim 1-9 any one.
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