Extraction thickener
Technical Field
The utility model relates to an extract concentrator, a draw concentrated machine specifically says so that one kind that the bioengineering field used.
Background
In the bioengineering field, often use and draw concentrator, carry out the extraction concentration of target product to the target product, current extraction concentrator has following defect:
1. the extraction and concentration need separate work and cannot be carried out simultaneously;
2. the extracted target product is single, and the extraction and concentration of various target products cannot be realized;
3. the extraction concentration rate of the target product is low, and the utilization rate of raw materials is low.
The defects limit the upgrading and updating of the extraction and concentration equipment and cannot meet the extraction and concentration requirements of production enterprises for various products.
Disclosure of Invention
The utility model aims at providing an extract concentrated machine.
In order to achieve the above purpose, the technical scheme of the utility model is that: an extraction concentrator comprises a separation system, an extraction system, a concentration system, a condensation system and a transportation system, wherein the condensation system comprises a first condenser, a second condenser, a plurality of groups of first condenser pipelines and a plurality of groups of second condenser pipelines, the transportation system comprises a plurality of groups of material transportation pipelines, a water transportation pipeline, a vacuum pump, a filter, a material pump and a gas transportation pipeline, the separation system and the extraction system are connected and installed through the material transportation pipeline, the water transportation pipeline and the first condenser as well as the first condenser pipeline installed on the first condenser, and the extraction system and the concentration system are connected and installed through the material transportation pipeline, the water transportation pipeline and the second condenser as well as the second condenser pipeline installed on the second condenser;
the separation system comprises a separator water storage tank, a separator, a liquid level meter, a water return pipe and a separator observation port, wherein the separator is installed at the top of the separator water storage tank, the liquid level meter is installed at the center of the right end face of the separator water storage tank, the water return pipe is installed on the outer side of the left upper corner of the separator water storage tank, the separator observation port is installed at the position, close to the top, of the front end face of the separator water storage tank, the top and the left end of the top of the separator are respectively connected with the right lower end of a first condenser and the left side position of the right lower end of the first condenser through two groups of first condenser pipelines, and a drain pipe is installed at;
the extraction system comprises an extraction tank body, an extraction tank cover, a first heating pipe and a first waste residue outlet, the top of the extracting tank body is provided with an extracting tank cover, the first heating pipes are arranged at the left end and the right end of the bottom of the extracting tank body, the first waste residue outlet is arranged at the lower position close to the center of the front end surface of the extracting tank body, a first condenser interface is arranged at the center of the top of the extraction tank cover, a water body transportation pipeline interface is arranged at the upper right part of the first condenser interface, an extracting solution outlet pipe is arranged at the center of the bottom of the extracting tank body, the first condenser and the first condenser interface are connected and arranged through a first condenser pipeline, the water body conveying pipeline interface is connected with the water discharge pipe through a water body conveying pipeline, the bottom of the separator is connected with a vacuum pump through a material conveying pipeline, and the left end of the vacuum pump is connected with the right lower end of the extraction tank body through a material conveying pipeline;
the bottom of the second condenser is connected with a second condenser water storage tank, a first condenser pipeline connected with the second condenser is installed near the left position of the top of the first condenser, the left end of the extracting solution outlet pipe is connected with a filter through a material conveying pipeline, and a second condenser pipeline connected with the right upper end of the second condenser water storage tank is installed on the left end face of the filter;
concentrated system includes the concentrated jar of normal atmospheric temperature and the concentrated jar of heating, the top of the concentrated jar of normal atmospheric temperature meets through the upper left end of second condenser pipeline with the second condenser, the bottom of filter and the concentrated jar right-hand member face of normal atmospheric temperature lean on to meet through material transport pipeline between the position, the bottom of the concentrated jar of normal atmospheric temperature is linked together through the right lower extreme of material transport pipeline with the concentrated jar of heating, the concentrated jar right-hand member face of heating is close to the top position and meets through the left end face of gas transport pipeline with the concentrated jar of normal atmospheric temperature, vertically installs two sets of concentrated jar viewing apertures of normal atmospheric temperature at the preceding terminal surface intermediate position of the concentrated jar of normal atmospheric temperature, installs the export of second waste residue in two sets of concentrated jar viewing apertures of normal atmospheric temperature, installs the concentrate exit tube at the bottom central point of the concentrated jar of heating, installs.
Preferably, a filling port is arranged at the lower left of the first condenser interface, a lighting device is arranged at the upper left, a pressure gauge and a deflation valve are arranged at the right, and an observation port of the extraction tank is arranged below the deflation valve.
Preferably, the filter comprises a main body, an end cover, a filter screen and a filter screen grate, wherein the end cover is installed at the top of the main body, a feed inlet is installed at the upper position of the right end face of the main body, the filter screen grate is installed on the inner wall of the main body below the feed inlet, and the filter screen extending to the bottom of the main body is installed on the inner side of the filter screen grate.
Preferably, an air inlet and a stop valve are arranged on a material conveying pipeline between the normal-temperature concentration tank and the heating concentration tank.
Preferably, a material pump is arranged on a material conveying pipeline between the filter and the second condenser.
Preferably, an oil outlet is installed at the left lower end of the first heating pipe.
Preferably, a silica gel sealing ring is embedded at the joint of the main body and the end cover.
Due to the adoption of the technical scheme, the beneficial effects of the utility model are that: the utility model adds two groups of condensers on the basis of the original extraction and concentration equipment, thus improving the working efficiency of the whole machine and realizing the synchronous operation of extraction and concentration; meanwhile, a filter is additionally arranged according to the extraction and concentration conditions of the product, the extraction and concentration rate of the product is improved, a heating and concentration tank is additionally arranged, the heating efficiency is improved, and the heating power is reduced. The utility model discloses can satisfy the demand of drawing of different products according to the condition of drawing, can reach energy-efficient target.
Drawings
The present invention will now be further described with reference to the accompanying drawings.
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic diagram of the structure of the separation system of the present invention.
Fig. 3 is a front view of the extraction system of the present invention.
Fig. 4 is a top view of the extraction system of the present invention.
Fig. 5 is a schematic diagram of the filter structure of the present invention.
Fig. 6 is the structure schematic diagram of the normal temperature concentration tank of the present invention.
Fig. 7 is a schematic structural view of the heating concentration tank of the present invention.
In the figure: 1. a separation system, 11, a separator water storage tank, 12, a separator, 13, a liquid level meter, 14, a water return pipe, 15, a separator observation port, 16, a drain pipe, 2, an extraction system, 21, an extraction tank body, 22, an extraction tank cover, 23, a first heating pipe, 24, a first waste residue outlet, 25, a first condenser interface, 26, a water body transportation pipeline interface, 27, an extract outlet pipe, 28, a filling port, 29, a lighting device, 210, a pressure gauge, 211, a vent valve, 212, an extraction tank observation port, 213, an oil outlet, 3, a concentration system, 31, a normal temperature concentration tank, 32, a heating concentration tank, 33, a normal temperature concentration tank observation port, 34, a second waste residue outlet, 35, a concentrated solution outlet pipe, 36, a second heating pipe, 37, an air inlet, 38, a stop valve, 4, a condensation system, 41, a first condenser, 42, a second condenser, 43, a first condenser pipeline, 44. second condenser pipeline, 45, second condenser water storage tank, 5, transportation system, 51, material transportation pipeline, 52, water transportation pipeline, 53, vacuum pump, 54, filter, 541, main body, 542, end cover, 543, filter screen, 544, filter screen grate, 545, feed inlet, 546, silica gel sealing ring, 55, material pump, 56 and gas transportation pipeline.
Detailed Description
The technical solution of the present invention will be described clearly and completely with reference to the accompanying drawings, and obviously, the described embodiments are some embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, it should be noted that, as the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. appear, the indicated orientation or positional relationship thereof is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, but does not indicate or imply that the indicated device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" as appearing herein are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" should be interpreted broadly, e.g., as being either fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.
As shown in fig. 1-7, the utility model relates to an extraction thickener, which comprises a separation system 1, an extraction system 2, a concentration system 3, a condensation system 4 and a transportation system 5, the condensing system 4 comprises a first condenser 41, a second condenser 42, a plurality of sets of first condenser tubes 43 and a plurality of sets of second condenser tubes 44, the transportation system 5 comprises a plurality of groups of material transportation pipelines 51, a water transportation pipeline 52, a vacuum pump 53, a filter 54, a material pump 55 and a gas transportation pipeline 56, the separation system 1 and the extraction system 2 are connected and installed through a material conveying pipeline 51, a water body conveying pipeline 52, a first condenser 41 and a first condenser pipeline 43 installed on the first condenser 41, the extraction system 2 and the concentration system 3 are connected and installed through a material conveying pipeline 51, a water body conveying pipeline 52, a second condenser 42 and a second condenser pipeline 44 installed on the second condenser 42;
the separation system 1 comprises a separator water storage tank 11, a separator 12, a liquid level meter 13, a water return pipe 14 and a separator observation port 15, wherein the separator 12 is installed at the top of the separator water storage tank 11, the liquid level meter 13 is installed at the central position of the right end face of the separator water storage tank 11, the water return pipe 14 is installed outside the upper left corner of the separator water storage tank 11, the separator observation port 15 is installed at the position, close to the top position, of the front end face of the separator water storage tank 11, the top and the left end of the top of the separator 12 are respectively connected with the right lower end of a first condenser 41 and the left side position of the right lower end through two groups of first condenser pipelines 43, and a water discharge pipe 16 is installed at the bottom of the separator water;
the extraction system 2 comprises an extraction tank body 21, an extraction tank cover 22, a first heating pipe 23 and a first waste residue outlet 24, wherein the extraction tank cover 22 is installed at the top of the extraction tank body 21, the first heating pipe 23 is installed at the left end and the right end of the bottom of the extraction tank body 21, the first waste residue outlet 24 is arranged at the lower position of the center of the front end surface of the extraction tank body 21, a first condenser interface 25 is arranged at the central position of the top of the extraction tank cover 22, a water body transportation pipeline interface 26 is installed at the upper right of the first condenser interface 25, an extraction liquid outlet pipe 27 is installed at the central position of the bottom of the extraction tank body 21, the first condenser 41 is connected with the first condenser interface 25 through a first condenser pipeline 43, the water body transportation pipeline interface 26 is connected with a water discharge pipe 16 through a water body transportation pipeline 52, the bottom of the separator 12 is connected with a vacuum pump 53 through a material, the left end of the vacuum pump 53 is connected with the right lower end of the extraction tank body 21 through a material conveying pipeline 51;
the bottom of the second condenser 42 is connected with a second condenser water storage tank 45, a first condenser pipeline 43 connected with the second condenser 42 is arranged close to the left position on the top of the first condenser 41, the left end of the extracting solution outlet pipe 27 is connected with a filter 54 through a material conveying pipeline 51, and the left end surface of the filter 54 is provided with a second condenser pipeline 44 connected with the right upper end of the second condenser water storage tank 45;
the concentration system 3 comprises a normal temperature concentration tank 31 and a heating concentration tank 32, the top of the normal temperature concentration tank 31 is connected with the left upper end of a second condenser 42 through a second condenser pipeline 44, the bottom of the filter 54 is connected with the upper position of the right end surface of the normal temperature concentration tank 31 through a material conveying pipeline 51, the bottom of the normal temperature concentration tank 31 is communicated with the right lower end of the heating concentration tank 32 through a material conveying pipeline 51, the right end surface of the heating concentration tank 32 close to the top is connected with the left end surface of the normal temperature concentration tank 31 through a gas conveying pipeline 56, two groups of normal temperature concentration tank observation ports 33 are longitudinally arranged at the middle position of the front end surface of the normal temperature concentration tank 31, a second waste residue outlet 34 is arranged below the two groups of normal temperature concentration tank observation ports 33, a concentrated solution outlet pipe 35 is arranged at the central position of the bottom of the heating concentration tank 32, and a second heating pipe 36 is arranged on the outer wall of the tank body of the heating concentration tank 32.
A filling port 28 is arranged at the lower left of the first condenser interface 25, a lighting device 29 is arranged at the upper left, a pressure gauge 210 and a release valve 211 are arranged at the right side, and an extraction tank observation port 212 is arranged below the release valve 211.
The filter 54 includes a main body 541, an end cover 542, a filtering screen 543 and a filtering screen grate 544, wherein the end cover 542 is installed at the top of the main body 541, a feeding hole 545 is installed at an upper position of the right end surface of the main body 541, the filtering screen grate 544 is installed on the inner wall of the main body 541 below the feeding hole 545, and the filtering screen 543 extending to the bottom of the main body 541 is installed at the inner side of the filtering screen grate 544.
An air inlet 37 and a stop valve 38 are arranged on the material conveying pipeline 51 between the normal temperature concentration tank 31 and the heating concentration tank 32.
A material pump 55 is mounted on the material conveying pipe 51 between the filter 54 and the second condenser 42.
An oil outlet 213 is installed at the left lower end of the first heating pipe 23.
And a silica gel sealing ring 546 is embedded at the joint of the main body 541 and the end cover 542.
The working principle is as follows: after the target product is effectively separated by the separator 12 and is mixed with water in the water storage tank 11 of the separator, a vacuum pump 53 provides power, mixed liquid is pumped into the extraction tank body 21 through a material conveying pipeline 51, the first heating pipe 23 heats the extraction tank body 21, target substances in the mixed liquid are separated and extracted, and a part of waste residues are discharged through a first waste residue outlet 24;
the target substance obtained by separation and extraction is dissolved in water and then enters a filter 54 through a material conveying pipeline 51, more impurities are filtered under the action of a filter screen 53 and a filter screen grate 54, the filtered mixed liquid enters a normal-temperature concentration tank 31 through the material conveying pipeline 51, a part of the mixed liquid enters a heating concentration tank 32 through the material conveying pipeline 51, heat is provided for a concentration system 3 by a second heating pipe 36 in the heating concentration tank 32, hot gas generated in the heating concentration tank 32 enters the normal-temperature concentration tank 31 through a gas conveying pipeline 56 to provide heat for the normal-temperature concentration tank 31, the concentration of the target product is accelerated, and the target product obtained by concentration finally flows out through a concentrated solution outlet pipe 35 and is collected.
In the above process, a part of the waste heat gas generated by heating enters the second condenser 42 through the second condenser pipeline 44, the condensed water enters the second condenser water storage tank 45 for collection, the other part enters the first condenser 41 through the first condenser pipeline 43 for condensation, and after condensation, the waste heat gas flows back to the separator water storage tank 11 through the first condenser pipeline 43 for collection, and finally is discharged through the water discharge pipe 16.
The foregoing is a detailed description of the present invention in connection with specific preferred embodiments, and it is not to be construed that the specific embodiments of the present invention are limited to those descriptions. To those skilled in the art to which the invention pertains, without departing from the spirit of the invention, several simple deductions or substitutions can be made, all of which should be considered as belonging to the scope of patent protection defined by the claims filed with the invention.