CN208894047U - It is a kind of for extracting the dissolution enrichment facility of gangliosides - Google Patents

It is a kind of for extracting the dissolution enrichment facility of gangliosides Download PDF

Info

Publication number
CN208894047U
CN208894047U CN201821306789.3U CN201821306789U CN208894047U CN 208894047 U CN208894047 U CN 208894047U CN 201821306789 U CN201821306789 U CN 201821306789U CN 208894047 U CN208894047 U CN 208894047U
Authority
CN
China
Prior art keywords
steam
condensing unit
dissolution
cooling device
outlet
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
Application number
CN201821306789.3U
Other languages
Chinese (zh)
Inventor
向家兵
向加刚
张宇
王龙军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan Xingjixiang Pharmaceutical Co Ltd
Original Assignee
Sichuan Xingjixiang Pharmaceutical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sichuan Xingjixiang Pharmaceutical Co Ltd filed Critical Sichuan Xingjixiang Pharmaceutical Co Ltd
Priority to CN201821306789.3U priority Critical patent/CN208894047U/en
Application granted granted Critical
Publication of CN208894047U publication Critical patent/CN208894047U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Fats And Perfumes (AREA)

Abstract

The utility model discloses a kind of for extracting the dissolution enrichment facility of gangliosides, including agitator tank, driving motor, agitating shaft, blade, steam pipeline, condensing unit, cooling device, drain pipe, oil water separator and support frame are mixed, the agitator tank and condensing unit are each attached on support frame;The cover is equipped with material inlet and steam (vapor) outlet;Tank wall is equipped with heating interlayer, and heating interlayer inner wall is equipped with temperature sensor;Described steam pipeline one end is connected with steam (vapor) outlet, and the other end is connected with condensing unit;The condensing unit end is equipped with drain pipe, and the drain pipe is connected with cooling device side wall.The utility model belongs to animals and plants byproduct and extracts field, heating temperature can not only be controlled, guarantee heating stirring efficiency when extracting Ganglioside, a cooling device can also be added outside condensing unit, while reinforcing steam cooling, the safety for also ensuring whole device substantially reduces the time of dissolution concentration.

Description

It is a kind of for extracting the dissolution enrichment facility of gangliosides
Technical field
The utility model relates to the technical fields that animals and plants beneficiating ingredient extracts, and in particular to one kind is for extracting neuromere The dissolution enrichment facility of glycosides rouge.
Background technique
Animals and plants byproduct refer to poultry, domestic animal, the bone of aquatic products, internal organ, fat, marrow, root, stem, leaf etc. not by The part that the mankind eat or utilize, these products but contain a large amount of beneficiating ingredient, people would generally be driven despite byproduct It extracts beneficiating ingredient in plant by-product to use as him, to meet the various needs of people.
In pharmaceutical industry or laboratory, it usually needs extract the beneficiating ingredient in animals and plants byproduct, use To prepare medicinal material or carry out related experiment;Gangliosides are a kind of acidic glycosphingolipids substances for being present in cell membrane surface, Just be found and gain the name in nerve cell early in 1940, content is the abundantest in nervous system for it, be also present in spleen and It is a kind of most complicated glycosphingolipids substance in red blood cell;Ganglioside is by extracting in animal brain, generally It is extracted from pig brain, pig brain is the starting material for producing gangliosides, and the gangliosides for extracting 1kg usually require tons of Pig brain, in process of production, how the pig brain of such flood tide, which effectively blends and be concentrated, sufficiently directly affects gangliosides Yield and production cost;It nowadays is to use the processes such as stirring, heating, cooling concentration to the extraction of gangliosides, When being stirred to pig brain, heating temperature can not be controlled, for temperature too down to less than preferable extraction effect, temperature is too high It is be easy to cause the damage of substance, leverages the quality of extraction, and is condensed using steam of the condensing unit to extraction When, since the path that steam can pass through in condensing unit is more, steam can still exist less after condensing unit condenses The not cooled steam of amount, steam is " vapour locking " easy to form in the duct, so as to cause positive pressure is formed in tank, brings certain Risk is given in usual operating process, needs to empty or reduce the temperature of heating, and the effect for causing dissolution to be concentrated in this way is not Good, the time is longer.
Utility model content
For the existing deficiency for extracting Ganglioside device, the purpose of this utility model is that proposing a kind of for mentioning The dissolution enrichment facility of gangliosides is taken, which can not only control the temperature of heating, guarantee to extract neuromere former times Heating stirring efficiency when rouge, and by adding a cooling device again in condensing unit outer end, reinforcing steam cooling Meanwhile also ensuring the safety of whole device, substantially reduce the time of dissolution concentration.
To achieve the above object, the technical scheme adopted by the utility model is
It is a kind of for extracting the dissolution enrichment facility of gangliosides, including agitator tank, steam pipeline, condensing unit, Cooling device, drain pipe and support frame, the agitator tank and condensing unit are each attached on support frame;
The agitator tank includes tank body and cover, and driving motor, the driving motor lower section are equipped with right above the cover It is connected with agitating shaft, the agitating shaft protrudes into tank interior, and the agitating shaft is equipped with stirring blade;The cover is equipped with original Material feed inlet and steam (vapor) outlet, the steam (vapor) outlet are connected with steam pipeline;The tank wall is equipped with heating interlayer, described Heating interlayer outer wall be equipped with water inlet of hot water, heating interlayer bottom be equipped with hot water outlet, the heating interlayer inner wall be equipped with pair The temperature sensor that heating temperature is detected;The tank base is equipped with bottom valve;
Described steam pipeline one end is connected with steam (vapor) outlet, and the other end is connected with condensing unit;
The condensing unit end is equipped with drain pipe, and the drain pipe is connected with cooling device side wall;The cooling device Top is equipped with cooling water inlet pipe, and bottom is equipped with cooling water outlet pipe, the condenser pipe of the cooling water inlet pipe and condensing unit It is connected;The cooling device is connected to agitator tank by liquid delivery tube, and the liquid delivery tube is equipped with oil water separator, institute The liquid delivery tube stated between oil water separator and agitator tank is equipped with visible observation section.
Further, the cooling device carries out hot friendship by the hot steam of uncooled completion inside cold water and drain pipe It changes;Not condensed complete hot steam continues to cool down in cooling device in condensing unit, avoids hot steam in pipeline Occur " vapour locking ", improves the efficiency of dissolution concentration.
Further, being equipped with fuel-displaced valve at the liquid outlet of the oil water separator;Oil water separator is carrying out grease After separation, grease is discharged from fuel-displaced valve.
Further, the thickness of the heating interlayer is uniform;It ensure that being evenly heated for various pieces in agitator tank, mention The quality of high stirring and dissolving.
Further, the condensing unit side wall is equipped with cold water inlet.
Further, support frame as described above bottom is equipped with castor;The device, which facilitates, to be moved, and use is very flexible.
Further, the visible observation section is thermostable transparent pipeline.
The beneficial effects of the utility model are:
The utility model structure is simple, when carrying out heating stirring dissolution, can not only realize stirring tank wall heating temperature It is uniform, can also realize detection to heating interlayer internal hot-water temperature by temperature sensor, guarantee heating temperature be in plus Hot pig brain extracts the optimum temperature range of gangliosides, reduces damage of the high temperature to pig brain, also avoids low temperature effect dissolution dense The efficiency of contracting is supervised when being adjusted to heating temperature by heating temperature of the temperature sensor to heating interlayer in real time Control, guarantees the accuracy of heating temperature, when the temperature inside heating interlayer changes, can be issued by temperature sensor Information is regulated and controled;
A cooling device, the not condensed steaming finished in condensing unit have been added after the condensing unit of the utility model Vapour and it is cooled after liquid all pass through the cooling device, the steam that finishes not condensed in condensing unit can be carried out again Secondary cooling improves the efficiency of cooling concentration, avoids steam that " vapour locking " occurs in the duct, ensure that the safety of device operation, Compared with the heating temperature for not having to empty or reduce repeatedly heating interlayer repeatedly in operation, when substantially reducing dissolution concentration Between, improve the efficiency of dissolution concentration;Oil water separator separates the grease in liquid, by visible observation section to liquid Liquid inside delivery pipe is observed, can if discovery still has a large amount of not cooled steam in visible observation section The appropriate temperature for reducing heating, is further ensured that the efficiency and safety of dissolution concentration;
And the device is movable, is facilitated by castor and is moved.
Detailed description of the invention
Fig. 1 is the complete structure schematic diagram of the utility model.
In figure: 1, cover;2, agitating shaft;3, stirring blade;4, temperature sensor;5, tank body;6, castor;7, hot water goes out The mouth of a river;8, bottom valve;9, heating interlayer;10, water inlet of hot water;11, support frame;12, fuel-displaced valve;13, liquid delivery tube; 13-1, visible observation section;14, oil water separator;15, cooling device;16, drain pipe;17, material inlet;18, driving electricity Machine;19, steam (vapor) outlet;20, condensing unit;21, cold water inlet;22, steam pipeline.
Specific embodiment
It is practical new to this with reference to the accompanying drawing in order to keep the purpose of this utility model, technical solution and advantage clearer Type is further elaborated.
In the present embodiment, as shown in Figure 1, it is a kind of for extracting the dissolution enrichment facility of gangliosides, including stirring Tank, steam pipeline 22, condensing unit 20, cooling device 15, drain pipe 16 and support frame 11, the agitator tank and condensing unit 20 are each attached on support frame 11;The agitator tank includes tank body 5 and cover 1, is equipped with driving motor right above the cover 1 18, agitating shaft 2 is connected with below the driving motor 18, and the agitating shaft 2 protrudes into inside tank body 5, and the agitating shaft 2 is equipped with Stirring blade 3;The cover 1 is equipped with material inlet 17 and steam (vapor) outlet 19, the steam (vapor) outlet 19 and steam pipeline 22 are connected;5 outer wall of tank body is equipped with heating interlayer 9, and 9 outer wall of heating interlayer is equipped with water inlet of hot water 10, heating interlayer 9 Bottom is equipped with hot water outlet 7, and 9 inner wall of heating interlayer is equipped with the temperature sensor 4 detected to heating temperature, in order to It ensure that being evenly heated for various pieces in agitator tank, improve the quality of stirring and dissolving, the thickness of the heating interlayer 9 is uniform; 5 bottom of tank body is equipped with bottom valve 8;
Described 22 one end of steam pipeline is connected with steam (vapor) outlet 19, and the other end is connected with condensing unit 20;The condensation 20 end of device is equipped with drain pipe 16, and the drain pipe 16 is connected with 15 side wall of cooling device;It is set at the top of the cooling device 15 There is cooling water inlet pipe, bottom is equipped with cooling water outlet pipe, and the cooling water inlet pipe is connected with the condenser pipe of condensing unit 20, The cooling device 15 carries out heat exchange by the hot steam of the uncooled completion of cold water and the inside of drain pipe 16, in condensing unit 20 Not condensed complete hot steam continues to cool down in cooling device 15, avoids hot steam that " vapour locking " occurs in pipeline, Improve the efficiency of dissolution concentration;The cooling device 15 is connected to agitator tank by liquid delivery tube 13, the liquid conveying Pipe 13 is equipped with oil water separator 14, and the liquid delivery tube 13 between the oil water separator 14 and agitator tank is equipped with visual see Section 13-1 is examined, the visible observation section 13-1 is thermostable transparent pipeline;It is equipped at the liquid outlet of the oil water separator 14 Oil valve door 12;It can be observed by visible observation section 13-1 cooling liquid has been completed, if discovery visible observation section 13- There are still a large amount of not cooled steam in 1, the temperature of heating can be reduced in right amount.
As a kind of prioritization scheme of the utility model, 20 side wall of condensing unit is equipped with cold water inlet 21.
As a kind of prioritization scheme of the utility model, 11 bottom of support frame as described above is equipped with castor 6;The castor 6 It is equipped with brake gear;The device, which facilitates, to be moved, and use is very flexible.
Using the utility model when extracting gangliosides by pig brain, use process is as follows, first to the device All parts, each tank body, local part are overhauled, and guarantee that the device can operate normally, and avoid that safety accident occurs when operation; When in use, pig brain is added into material inlet 17, opens driving motor 18, driving motor 18 drives agitating shaft 2 to rotate, stirs Mixing axis 2 drives stirring blade 3 to be stirred the pig brain in tank body 5;Pass through in water inlet of hot water 10 simultaneously into heating interlayer 9 Hot water is added, the pig brain inside tank body 5 is heated by the hot water in heating interlayer 9, accelerates the neuromere in pig brain The dissolution of glycosides rouge ingredient is leached;The temperature inside heating interlayer 9 is carried out by the temperature sensor 4 of 9 inner wall of heating interlayer real When monitor, guarantee heating temperature be in be most suitable for gangliosides leach temperature range, avoid temperature it is excessively high cause pig brain or The damage of gangliosides avoids the too low extraction dissolved efficiency for influencing gangliosides of temperature;
After by heating stirring, the effective components such as gangliosides being precipitated from pig brain pass through as a vapor Steam (vapor) outlet 19 is sent into condensing unit 20 by steam pipeline 22 and is condensed, and condensation finishes the liquid to be formed or uncooled complete Complete residual steam is entered in cooling device 15 by drain pipe 16, and cooling device 15 is finished not condensed in condensing unit 20 Steam cooled down again, avoid steam from forming " vapour locking " in pipeline, ensure that the safety of device operation, compared with not having to The heating temperature for emptying or reducing repeatedly heating interlayer 9 repeatedly in operation substantially reduces dissolution concentration time, improves The efficiency of dissolution concentration;Oil water separator 14 separates the oil in liquid, while can also pass through visible observation section 13- It has completed cooling liquid for 1 pair to observe, if there are still a large amount of not cooled in discovery visible observation section 13-1 Steam can reduce the temperature of heating in right amount, be further ensured that the efficiency and safety of dissolution concentration;The finally liquid after supercooling Body, which is again introduced into inside agitator tank, carries out circulating-heating stirring, finally extracts from the bottom valve of agitator tank 8 by required concentrate Out.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above.Current row The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model Claimed range is defined by the appending claims and its equivalent thereof.

Claims (7)

1. a kind of for extracting the dissolution enrichment facility of gangliosides, it is characterised in that: including agitator tank, steam pipeline (22), condensing unit (20), cooling device (15), drain pipe (16) and support frame (11), the agitator tank and condensing unit (20) it is each attached on support frame (11);
The agitator tank includes tank body (5) and cover (1), is equipped with driving motor (18) right above the cover (1), the driving It is connected with agitating shaft (2) below motor (18), the agitating shaft (2) protrudes into tank body (5) inside, and the agitating shaft (2) is equipped with Stirring blade (3);The cover (1) be equipped with material inlet (17) and steam (vapor) outlet (19), the steam (vapor) outlet (19) and Steam pipeline (22) is connected;Tank body (5) outer wall is equipped with heating interlayer (9), and heating interlayer (9) outer wall is equipped with hot water Water inlet (10), heating interlayer (9) bottom are equipped with hot water outlet (7), and heating interlayer (9) inner wall is equipped with to heating temperature The temperature sensor (4) detected;Tank body (5) bottom is equipped with bottom valve (8);
Described steam pipeline (22) one end is connected with steam (vapor) outlet (19), and the other end is connected with condensing unit (20);
Condensing unit (the 20)-end is equipped with drain pipe (16), the drain pipe (16) and cooling device (15) side wall phase Even;Cooling water inlet pipe is equipped at the top of the cooling device (15), bottom is equipped with cooling water outlet pipe, the cooling water inlet pipe It is connected with the condenser pipe of condensing unit (20);The cooling device (15) is connected to agitator tank by liquid delivery tube (13), institute The liquid conveying that liquid delivery tube (13) are stated equipped with oil water separator (14), between the oil water separator (14) and agitator tank It manages (13) and is equipped with visible observation section (13-1).
2. dissolution enrichment facility according to claim 1, it is characterised in that: the cooling device (15) passes through cold water and row The hot steam of the internal uncooled completion of liquid pipe (16) carries out heat exchange.
3. dissolution enrichment facility according to claim 2, it is characterised in that: at the liquid outlet of the oil water separator (14) Equipped with fuel-displaced valve (12).
4. dissolution enrichment facility according to claim 3, it is characterised in that: the thickness of the heating interlayer (9) is uniform.
5. dissolution enrichment facility according to claim 4, it is characterised in that: condensing unit (20) side wall is equipped with cold water Water inlet (21).
6. dissolution enrichment facility according to claim 5, it is characterised in that: support frame as described above (11) bottom is equipped with castor (6)。
7. dissolution enrichment facility according to claim 6, it is characterised in that: the visible observation section (13-1) is high temperature resistant Transparent pipeline.
CN201821306789.3U 2018-08-14 2018-08-14 It is a kind of for extracting the dissolution enrichment facility of gangliosides Active CN208894047U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821306789.3U CN208894047U (en) 2018-08-14 2018-08-14 It is a kind of for extracting the dissolution enrichment facility of gangliosides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821306789.3U CN208894047U (en) 2018-08-14 2018-08-14 It is a kind of for extracting the dissolution enrichment facility of gangliosides

Publications (1)

Publication Number Publication Date
CN208894047U true CN208894047U (en) 2019-05-24

Family

ID=66569182

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821306789.3U Active CN208894047U (en) 2018-08-14 2018-08-14 It is a kind of for extracting the dissolution enrichment facility of gangliosides

Country Status (1)

Country Link
CN (1) CN208894047U (en)

Similar Documents

Publication Publication Date Title
CN107413069A (en) Chinese medicine extracting tank
CN202478644U (en) Soxhlet extractor with stirring function
CN208894047U (en) It is a kind of for extracting the dissolution enrichment facility of gangliosides
CN210612903U (en) Novel ball-type concentrator is used in medicine subsides production
CN208493315U (en) A kind of extraction device for formulating of oral solution production
CN101564403A (en) Method for extracting and processing medicinal fungus water
CN207627977U (en) A kind of Chinese medicine concentrating tank with density measurement
CN206577417U (en) A kind of traditional Chinese medicine extraction separator
CN207276584U (en) A kind of fragrant plant hydrosol extraction of essential oil system
CN207614401U (en) A kind of traditional Chinese medicine extraction separator
CN106243217B (en) A kind of production system and preparation process being applicable in Yolk antibody
CN206473915U (en) Agitation and filtration all-in-one is used in a kind of honey manufacture
CN209952287U (en) Extraction element for pharmacy
CN101401818A (en) Sada mechanized forging process
CN209500868U (en) Active ingredients from traditional Chinese medicinal extraction system
CN206027151U (en) Jar is extracted with medicinal material to precious production of watermelon frost aditus laryngis
CN209612264U (en) A kind of traditional Chinese medicine extraction device
CN211097630U (en) Device for extracting cubilose acid from cubilose
CN210302451U (en) Double-effect concentration device for traditional Chinese medicine
CN207987194U (en) A kind of device for fermenting crops straws production biogas
CN207694374U (en) A kind of quick equipment for separating liquid from solid of Chinese medicine
CN208927995U (en) A kind of medicinal water numerical control agitating device
CN202369590U (en) Equipment for preparing composite calcium bilirubinate by using fermented ox bile
CN213771943U (en) Essence active ingredient draws jar
CN107469401B (en) Plant processing equipment capable of circularly extracting natural active ingredients of plants

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant