CN213644322U - Octopus raw material processing waste separating and extracting device - Google Patents

Octopus raw material processing waste separating and extracting device Download PDF

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Publication number
CN213644322U
CN213644322U CN202021888743.4U CN202021888743U CN213644322U CN 213644322 U CN213644322 U CN 213644322U CN 202021888743 U CN202021888743 U CN 202021888743U CN 213644322 U CN213644322 U CN 213644322U
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tank body
inner tank
outer tank
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material processing
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刘洪敏
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Laiyang Xinlonghai Food Co ltd
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Laiyang Xinlonghai Food Co ltd
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Abstract

The utility model relates to the technical field of marine product waste utilization, in particular to an octopus raw material processing waste separation and extraction device, which comprises a crushing device, a vacuum pulse extraction device, a filtering device and a vacuum decompression concentrator which are sequentially connected by pipelines; the smashing device comprises a base, an outer tank body is installed on the base, an inner tank body with a lower opening is sleeved in the outer tank body, the inner tank body is rotatably connected with the outer tank body, a backflow port is formed in the upper portion of the inner tank body, a backflow channel is formed between the outer tank body and the inner tank body, a liquid lifting device is arranged in the backflow channel, a bidirectional stirring device is installed in the inner tank body, and an airflow heating device is arranged in the outer tank body. Compared with the prior art, the utility model discloses utilize the marine product processing accessory substance to extract taurine, not only raw materials sources is safe, still can improve the utilization ratio of ocean resources, reduces environmental pollution, has solved that the synthetic method raw materials toxicity is big, the production facility investment is high and fermentation process output is low, and the technology route is long, the high problem of production facility investment.

Description

Octopus raw material processing waste separating and extracting device
Technical Field
The utility model relates to a marine product discarded object utilization technical field, in particular to octopus raw materials processing discarded object separation extraction element.
Background
The marine animal bodies have proved to contain rich taurine, and the existing devices for extracting taurine are all separation or refining devices for preparing taurine by chemical synthesis methods, and are not suitable for extracting taurine from the marine animal bodies (such as arca inflata, oysters, squids and the like). When the taurine is extracted by using marine organisms, a large amount of residual byproducts are often generated, and if the byproducts cannot be effectively treated, harmful microorganisms are easily bred, so that not only is the resource waste caused, but also the environmental pollution is also caused. At present, the natural taurine is mainly extracted by a boiling method, an ethanol extraction method, an enzymolysis method, an ultrasonic auxiliary extraction method and the like. The boiling method has the advantages of non-toxic reagent, simple process flow, low requirement on extraction equipment, low cost, small pollution and the like, is widely applied to the extraction of taurine in animals and plants, and has low yield. The method for preparing the taurine by the ethanol extraction method has the advantages that the obtained natural taurine has relatively single component, is beneficial to the separation and analysis of the taurine and convenient for the follow-up research, and has the defects of huge ethanol consumption and relatively low yield and purity of the natural taurine. The principle of the enzymolysis method is to utilize protease to destroy the structure of cell membrane and promote the dissolution of taurine in tissue cells in solvent so as to achieve the extraction and separation of products. The method has the advantages of mild extraction conditions, less side reactions in the extraction process, higher requirements on temperature and the addition of enzyme, higher price of protease and higher production cost.
SUMMERY OF THE UTILITY MODEL
For solving the technical problem, the utility model provides an octopus raw materials processing discarded object separation extraction element when extracting taurine in the octopus raw materials discarded object recycle residual material to realize the improvement of added value.
The utility model adopts the technical scheme as follows: octopus raw materials processing discarded object separation extraction element, the key lies in: comprises a crushing device, a vacuum pulse extraction device, a filtering device and a vacuum decompression concentrator which are sequentially connected by pipelines; the smashing device comprises a base, an outer tank body is installed on the base, an inner tank body with a lower opening is sleeved in the outer tank body, the inner tank body is connected with the outer tank body in a rotating mode, a backflow port is formed in the upper portion of the inner tank body, a backflow channel is formed between the outer tank body and the inner tank body, a liquid lifting device is arranged in the backflow channel, a bidirectional stirring device is installed in the inner tank body, and an airflow heating device is arranged in the outer tank body.
Preferably, the bidirectional stirring device comprises an upper rotating motor arranged at the top of the inner tank body and a lower rotating motor arranged on the base, the upper rotating motor is connected with the base through a support frame, an output shaft of the lower rotating motor penetrates into a fixedly connected stirring shaft in the inner tank body, a plurality of dispersion discs are fixedly sleeved on the stirring shaft, a plurality of dispersion blades are arranged on the inner wall of the inner tank body, and the dispersion blades are positioned between the adjacent dispersion discs.
Preferably, the airflow heating device comprises an annular air pipe and an air heater, the annular air pipe is located under the inner tank body, a plurality of air nozzles are arranged on the annular air pipe, and the air inlet end of the annular air pipe is communicated with the air heater pipeline.
Preferably, the liquid lifting device comprises a lifting motor arranged on the outer tank body, a mounting hole is formed in the upper portion of the outer tank body and is located above the backflow port, a lifting impeller is installed in the mounting hole, and the lifting impeller is connected with the lifting motor through a transmission shaft.
Preferably, the top of the inner tank body is provided with a feed inlet and a pressure reducing valve, and the lower part of the outer tank body is provided with a discharge outlet.
Preferably, the filtering device comprises two filtering cartridges arranged in parallel, and a filter bag is arranged at a liquid inlet of each filtering cartridge.
Preferably, the vacuum pulse extraction device comprises two extraction tanks which are arranged in parallel, and the two extraction tanks are respectively communicated with the same vacuum pump pipeline through a three-way valve.
Preferably, a flow meter is arranged between the filtering device and the vacuum decompression concentrator.
Has the advantages that: compared with the prior art, the octopus raw material processing waste separating and extracting device provided by the utility model has the advantages of reasonable design and convenient operation and use, the marine product waste can be fully and mechanically crushed by the crushing device, adhesion and blocking caused by the traditional heating mode are avoided, the uniformity and comprehensiveness of heating are ensured, the raw material in the tank is ensured to be rapidly heated, the stirring process is uniformly heated, the heat utilization rate is high, and the working efficiency is improved; the bidirectional stirring device can form turbulent flow on materials in the tank body, improve the dispersion efficiency, form upward suction force on the materials in the backflow channel by lifting the impeller, promote the materials to circularly flow between the inner tank body and the outer tank body, reduce the pressure in the tank body and improve the production safety; the vacuum pulse extraction device adopts low-temperature heating-vacuum-pulse, so that the structure that the extracting agent can deeply penetrate into the raw material improves the wetting and the impregnation of the raw material, a small amount of extracting agent is adopted, a more effective and strong extraction effect is achieved, and the total yield of the bioactive agent is improved; the utility model discloses can utilize the marine product processing accessory substance to draw taurine, not only raw materials sources is safe, still can improve the utilization ratio of ocean resource, reduces environmental pollution, has solved that synthetic method raw materials toxicity is big, production facility investment is high, environmental pollution, process operation are complicated and fermentation rule output is low, and the product needs further purification, and the process route is long, the high problem of production facility investment.
Drawings
Fig. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic structural view of the crushing apparatus.
Detailed Description
In order to make the technical solution of the present invention better understood by those skilled in the art, the present invention will be described in detail with reference to the accompanying drawings and the detailed description.
As shown in fig. 1-2, the separation and extraction device for octopus raw material processing waste comprises a crushing device a, a vacuum pulse extraction device c, a filtering device and a vacuum decompression concentrator d which are sequentially connected by pipelines, the vacuum pulse extraction device c comprises two extraction tanks c1 which are arranged in parallel, the feed inlets of the extraction tanks c1 are respectively connected with the discharge outlet pipelines of the crushing device a, the discharge port of the extracting tank c1 is connected with the feed port of the filtering device through a pipeline, the air outlets of the two extracting tanks c1 are respectively communicated with the same vacuum pump c3 through a three-way valve c2, the filtering device comprises two filtering cylinders b1 which are arranged in parallel, a filtering bag is arranged at the liquid inlet of the filtering cylinder b1, the reflux pump e is arranged between the filtering device and the vacuum decompression concentrator d, and a flowmeter f is arranged between the filtering device and the reflux pump e;
as can be seen in fig. 2, the pulverizing device a includes a base a1, an outer tank a2 is mounted on the base a1, an inner tank a3 with a lower opening is sleeved in the outer tank a2, the inner tank a3 is rotatably connected with the outer tank a2, a feed inlet a31 and a pressure reducing valve a32 are opened at the top of the inner tank a3, a discharge outlet a22 is opened at the lower part of the outer tank a2, a return outlet a4 is opened at the upper part of the inner tank a3, a return channel is formed between the outer tank a2 and the inner tank a3, a liquid lifting device a5 is arranged in the return channel, an upper rotating motor a7 is mounted at the top of the inner tank a3, the upper rotating motor a7 is connected with the base a1 by a support frame, a lower rotating motor a8 is mounted at the lower surface of the base a1, the rotating motor a8, an output shaft of the lower rotating motor a8 vertically penetrates upwards into the inner tank a3 and is fixedly connected with a9, a plurality of dispersion discs a10 are fixedly sleeved on the stirring shaft a9, a plurality of dispersion blades a11 are arranged on the inner wall of the inner tank a3, the dispersion blades a11 are positioned between the adjacent dispersion discs a10, and an airflow heating device a6 is arranged in the outer tank a 2;
the air flow heating device a6 comprises an annular air pipe a61 and a hot air blower a62, wherein the annular air pipe a61 is positioned right below the inner tank body a3, a plurality of air nozzles a63 are arranged on the annular air pipe a61, and the air inlet end of the annular air pipe a61 is communicated with a pipeline of the hot air blower a 62; the liquid lifting device a5 comprises a lifting motor a51 arranged on the outer tank a2, a mounting hole is formed in the upper portion of the outer tank a2 and located above the return port a4, a lifting impeller a52 is installed in the mounting hole, and the lifting impeller a52 is connected with the lifting motor a51 through a transmission shaft.
When in use, marine product waste is put into an inner tank a3 of a crushing device a, raw materials are effectively dispersed by reversely rotating a dispersion disc a10 and a dispersion blade a11, hot air is continuously introduced through an air heater a62, the materials in the tank can be heated, the stirring process is uniformly heated, the heat utilization rate is high, the working efficiency is high, the working time is shortened, the material in a backflow channel is circularly flowed in an inner tank a3 and an outer tank a2 by increasing the upward lifting force of an impeller a52, the dispersion efficiency is further improved, the materials are fully crushed into slurry, the slurry enters an extraction tank c1 through a pipeline, the pulse vacuum treatment of the mixture is carried out according to set parameters, the vacuum rate in the extraction tank c1 is adjusted to 1.3Kpa, the pulse duration time is 0.5-1.0 second in total, the slurry is subjected to vacuum exposure for 1-5 minutes, and after the vacuum exposure of the mixture is completed, the rapid vacuum release is carried out through a three-way valve c2, the circulation is carried out for 3-5 times, the extraction is completed, then the extracted slurry enters a filter cylinder b1 through a pipeline for filtration, each filter cylinder b1 is switched (used for replacing filter bags) through a control valve, and the filtrate finally enters a vacuum decompression concentrator d for concentration by about 3 times and is discharged.
Finally, it should be noted that the above description is only a preferred embodiment of the present invention, and that those skilled in the art can make various similar representations without departing from the spirit and scope of the present invention.

Claims (8)

1. Octopus raw materials processing discarded object separation extraction element, its characterized in that: comprises a crushing device (a), a vacuum pulse extraction device (c), a filtering device and a vacuum decompression concentrator (d) which are sequentially connected by pipelines, a reflux pump (e) is arranged between the filtering device and the vacuum decompression concentrator (d), the crushing device (a) comprises a base (a1), an outer tank body (a2) is arranged on the base (a1), an inner tank body (a3) with a lower opening is sleeved in the outer tank body (a2), the inner tank body (a3) is rotatably connected with the outer tank body (a2), a backflow port (a4) is formed at the upper part of the inner tank body (a3), a backflow channel is formed between the outer tank body (a2) and the inner tank body (a3), a liquid lifting device (a5) is arranged in the backflow channel, a bidirectional stirring device is arranged in the inner tank body (a3), and an air flow heating device (a6) is arranged in the outer tank body (a 2).
2. The octopus raw material processing waste separating and extracting device as claimed in claim 1, wherein: the bidirectional stirring device comprises an upper rotating motor (a7) arranged at the top of the inner tank body (a3) and a lower rotating motor (a8) arranged on a base (a1), wherein the upper rotating motor (a7) is connected with the base (a1) through a supporting frame, the lower rotating motor (a8) is arranged on the lower surface of the base (a1), an output shaft of the lower rotating motor (a8) vertically penetrates into the inner tank body (a3) upwards and is fixedly connected with a stirring shaft (a9), the stirring shaft (a9) is fixedly sleeved with a plurality of dispersion discs (a10), the inner wall of the inner tank body (a3) is provided with a plurality of dispersion blades (a11), and the dispersion blades (a11) are positioned between the adjacent dispersion discs (a 10).
3. The octopus raw material processing waste separating and extracting device as claimed in claim 1, wherein: the air flow heating device (a6) comprises an annular air pipe (a61) and a hot air blower (a62), wherein the annular air pipe (a61) is located under the inner tank body (a3), a plurality of air nozzles (a63) are arranged on the annular air pipe (a61), and the air inlet end of the annular air pipe (a61) is communicated with a pipeline of the hot air blower (a 62).
4. The octopus raw material processing waste separating and extracting device as claimed in claim 3, wherein: the liquid lifting device (a5) comprises a lifting motor (a51) arranged on the outer tank body (a2), a mounting hole is formed in the upper portion of the outer tank body (a2), the mounting hole is located above the backflow port (a4), a lifting impeller (a52) is installed in the mounting hole, and the lifting impeller (a52) is connected with the lifting motor (a51) through a transmission shaft.
5. The octopus raw material processing waste separating and extracting device as claimed in claim 3, wherein: the top of the inner tank body (a3) is provided with a feed inlet (a31) and a pressure reducing valve (a32), and the lower part of the outer tank body (a2) is provided with a discharge outlet (a 22).
6. The octopus raw material processing waste separating and extracting device as claimed in claim 1, wherein: the filtering device comprises two filtering cartridges (b1) arranged in parallel, and a filter bag is arranged at a liquid inlet of each filtering cartridge (b 1).
7. The octopus raw material processing waste separating and extracting device as claimed in claim 1, wherein: the vacuum pulse extraction device (c) comprises two extraction tanks (c1) which are arranged in parallel, and the two extraction tanks (c1) are respectively communicated with the same vacuum pump (c3) through three-way valves (c 2).
8. The octopus raw material processing waste separating and extracting device as claimed in claim 1, wherein: and a flowmeter (f) is arranged between the filtering device and the reflux pump (e).
CN202021888743.4U 2020-09-02 2020-09-02 Octopus raw material processing waste separating and extracting device Active CN213644322U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202021888743.4U CN213644322U (en) 2020-09-02 2020-09-02 Octopus raw material processing waste separating and extracting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202021888743.4U CN213644322U (en) 2020-09-02 2020-09-02 Octopus raw material processing waste separating and extracting device

Publications (1)

Publication Number Publication Date
CN213644322U true CN213644322U (en) 2021-07-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202021888743.4U Active CN213644322U (en) 2020-09-02 2020-09-02 Octopus raw material processing waste separating and extracting device

Country Status (1)

Country Link
CN (1) CN213644322U (en)

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