CN114854542A - Biological culture system - Google Patents

Biological culture system Download PDF

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CN114854542A
CN114854542A CN202210781214.1A CN202210781214A CN114854542A CN 114854542 A CN114854542 A CN 114854542A CN 202210781214 A CN202210781214 A CN 202210781214A CN 114854542 A CN114854542 A CN 114854542A
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target gas
concentration
module
biological
unit
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侯枕岍
陆大愚
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Jiangsu Hengyi Biotechnology Co ltd
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Jiangsu Hengyi Biotechnology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/36Means for collection or storage of gas; Gas holders
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01GHORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G31/00Soilless cultivation, e.g. hydroponics
    • A01G31/02Special apparatus therefor
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01GHORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G7/00Botany in general
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01GHORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
    • A01G7/00Botany in general
    • A01G7/02Treatment of plants with carbon dioxide
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/30Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
    • C12M41/34Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M47/00Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/10Separation or concentration of fermentation products
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/20Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2

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Abstract

Embodiments of the present description provide a biological culture system, including: the device comprises a target gas enrichment module, a separation module and a biological culture module which are connected in sequence; the target gas enrichment module is used for obtaining target mixed gas; the separation module is used for separating the mixed gas to obtain a target gas; the target gas is transmitted to the biological culture module according to a preset concentration threshold value, so that the system can improve the utilization rate of the target gas and reduce energy loss.

Description

Biological culture system
Technical Field
The specification relates to the field of biological culture, in particular to a biological culture system.
Background
In large-scale cultivation of green plants, microalgae, the gases required for their growth are maximally utilized, for example: carbon dioxide, oxygen, nitrogen, and the like are necessary. In the prior art, when green plants and microalgae are cultured on a large scale, a special culture system is generally provided for a certain plant or microalgae because of different gas concentrations required by different kinds of plants and microalgae for growth, and the utilization rate of gas with the concentration not within the concentration range of the target plant or microalgae is not high.
Therefore, it is desirable to provide a biological growth system that improves the utilization of the target gas.
Disclosure of Invention
To address the deficiencies of existing biological growth systems, one of the embodiments herein provides a biological growth system. The system comprises: comprises a target gas enrichment module, a separation module and a biological culture module which are connected in sequence; the target gas enrichment module is used for obtaining mixed gas; the separation module is used for separating the mixed gas to obtain a target gas; and transmitting the target gas to the biological culture module according to a preset concentration threshold value.
In some embodiments, the biological growth module comprises a plurality of first growth units connected in series from high to low according to the preset concentration threshold via a main conduit, and the output of the separation module is connected to the input of each of the first growth units via a bypass conduit.
In some embodiments, the culture apparatus further comprises a plurality of second culture units connected in parallel to the plurality of first culture units, respectively.
In some embodiments, the output end of the separation module, the output end of each of the first culture unit and the second culture unit are provided with a target gas concentration detection device, and the target gas concentration detection device is used for detecting the target gas concentration output by the corresponding output end.
In some embodiments, transmitting the target gas to the biological culture module according to a preset concentration threshold comprises: step 1: judging whether the input target gas concentration value belongs to a target gas concentration interval of the current first culture unit, if so, executing the step 2, if so, executing the step 3, and if not, judging the next stage and executing the step 1; step 2: inputting the target gas to a current first culture unit; and step 3: and returning to the previous stage and executing the step 1.
In some embodiments, transmitting the target gas to the biological growth module according to a preset concentration threshold further comprises: and 4, step 4: judging whether the input target gas concentration value belongs to a target gas concentration interval of the first-stage first culture unit, if so, executing the step 5, if so, executing the step 6, and if not, returning to the enrichment module and executing the step 4; and 5: inputting the target gas to a first-stage first culture unit; step 6: after the air is introduced, step 4 is performed.
In some embodiments, the target gas enrichment module is configured to obtain the mixed gas specifically including:
the target gas enrichment module comprises a target gas selective permeation material;
in some embodiments, the target gas selective permeation material is a single pass material that divides the target gas enrichment module into a high concentration unit and a low concentration unit;
raw gas is fed from the low concentration unit, and first target gas is obtained in the high concentration unit through the target gas selective permeation material;
and adding an extraction substance into the high-concentration unit based on the first target gas to obtain a mixed gas.
In some embodiments, the target gas is carbon dioxide.
In some embodiments, the target gas selective permeation material comprises: one or more of microporous alumina, microporous carbon, microporous silica, microporous perovskite, zeolite, and hydrotalcite.
In some embodiments, the separation module comprises one or more of a condenser, a distiller, a compressor.
Drawings
The present description will be further explained by way of exemplary embodiments, which will be described in detail by way of the accompanying drawings. These embodiments are not intended to be limiting, and in these embodiments like numerals are used to indicate like structures, wherein:
FIG. 1 is a schematic diagram of an application scenario of a biological growth system according to some embodiments of the present disclosure;
FIG. 2 is a schematic diagram of a system architecture for a biological growth system, according to some embodiments of the present disclosure;
FIG. 3 is a schematic illustration of the connection of a first culture unit according to some embodiments of the present disclosure;
FIG. 4 is a schematic illustration of the connection of a second culture unit according to some embodiments of the present disclosure;
in the figure: 1. a target gas enrichment module; 2. a separation module; 3. a first culture unit; 4. a target gas concentration detection device; 5. a switching device; 6. a second culture unit.
Detailed Description
In order to more clearly illustrate the technical solutions of the embodiments of the present disclosure, the drawings used in the description of the embodiments will be briefly described below. It is obvious that the drawings in the following description are only examples or embodiments of the present description, and that for a person skilled in the art, the present description can also be applied to other similar scenarios on the basis of these drawings without inventive effort. Unless otherwise apparent from the context, or otherwise indicated, like reference numbers in the figures refer to the same structure or operation.
It should be understood that "system", "apparatus", "unit" and/or "module" as used herein is a method for distinguishing different components, elements, parts, portions or assemblies at different levels. However, other words may be substituted by other expressions if they accomplish the same purpose.
As used in this specification and the appended claims, the terms "a," "an," "the," and/or "the" are not intended to be inclusive in the singular, but rather are intended to be inclusive in the plural, unless the context clearly dictates otherwise. In general, the terms "comprises" and "comprising" merely indicate that steps and elements are included which are explicitly identified, that the steps and elements do not form an exclusive list, and that a method or apparatus may include other steps or elements.
Flow charts are used in this description to illustrate operations performed by a system according to embodiments of the present description. It should be understood that the preceding or following operations are not necessarily performed in the exact order in which they are performed. Rather, the various steps may be processed in reverse order or simultaneously. Meanwhile, other operations may be added to the processes, or a certain step or several steps of operations may be removed from the processes.
Fig. 1 is a schematic diagram of an application scenario 100 of a biological growth system according to some embodiments of the present disclosure.
As shown in fig. 1, application scenario 100 may include processing device 110, network 120, user terminal 130, storage device 140, and biological growth system 150.
In some embodiments, the processing device 110 may process information or data in the application scenario 100. For example, processing device 110 may send a control signal to a control module of biological growth system 150, which may control a sensing device to obtain a concentration of a target gas output by a separation module, which is delivered to the biological growth module according to a preset concentration threshold.
In some embodiments, the processing device 110 may be regional or remote. For example, processing device 110 may access information and/or profiles stored in user terminal 130 and storage device 140 via network 120. In some embodiments, processing device 110 may be directly connected to user terminal 130 and storage device 140 to access information and/or material stored therein. In some embodiments, the processing device 110 may execute on a cloud platform. For example, the cloud platform may include one or any combination of a private cloud, a public cloud, a hybrid cloud, a community cloud, a decentralized cloud, an internal cloud, and the like. In some embodiments, the processing device 110 may comprise a processor, which may comprise one or more sub-processors (e.g., a single core processing device or a multi-core processing device). Merely by way of example, a processor may include a Central Processing Unit (CPU), an Application Specific Integrated Circuit (ASIC), an Application Specific Instruction Processor (ASIP), a Graphics Processor (GPU), a Physical Processor (PPU), a Digital Signal Processor (DSP), a Field Programmable Gate Array (FPGA), a programmable logic circuit (PLD), a controller, a microcontroller unit, a Reduced Instruction Set Computer (RISC), a microprocessor, and the like or any combination thereof.
The network 120 may facilitate the exchange of data and/or information in the application scenario 100. In some embodiments, one or more components in application scenario 100 (e.g., processing device 110, user terminal 130, storage device 140, and biological growth system 150) may send data and/or information to other components in application scenario 100 via network 120. In some embodiments, the network 120 may be any type of wired or wireless network. For example, network 120 may include a cable network, a wired network, a fiber optic network, a telecommunications network, an intranet, the internet, a Local Area Network (LAN), a Wide Area Network (WAN), a Wireless Local Area Network (WLAN), a Metropolitan Area Network (MAN), a Public Switched Telephone Network (PSTN), a bluetooth network, a ZigBee network, a Near Field Communication (NFC) network, the like, or any combination thereof.
User terminal 130 may obtain information or data in application scenario 100 and the user (e.g., a user of biological growth system 150) may be a user of user terminal 130. For example, user terminal 130 may send control instructions to processing device 110 via network 120, and processing device 110 may control the delivery of the target gas via a control module of biological growth system 150 in accordance with the control instructions. In some embodiments, the user terminal 130 may include one or any combination of a mobile device, a tablet, a laptop, and the like. In some embodiments, the mobile device may include a wearable device, a smart mobile device, a virtual reality device, an augmented reality device, and the like, or any combination thereof.
In some embodiments, the storage device 140 may be connected to the network 120 to enable communication with one or more components of the application scenario 100 (e.g., the processing device 110, the user terminal 130, etc.). One or more components of the application scenario 100 may access material or instructions stored in the storage device 140 through the network 120. In some embodiments, the storage device 140 may be directly connected or in communication with one or more components (e.g., processing device 110, user terminal 130) in the application scenario 100. In some embodiments, the storage device 140 may be part of the processing device 110.
The biological cultivation system 150 is used to provide a specific concentration of a target gas to the cultivated plants or microalgae. The biological culture-based system 150 may exchange data and/or information with one or more components (e.g., the processing device 110, the user terminal 130, and the storage device 140) in the application scenario 100. For further description of biological growth system 150, reference is made to FIG. 2 and its associated description.
It should be noted that the foregoing description is provided for illustrative purposes only, and is not intended to limit the scope of the present application. Many variations and modifications will occur to those skilled in the art in light of the teachings herein. The features, structures, methods, and other features of the exemplary embodiments described herein may be combined in various ways to obtain additional and/or alternative exemplary embodiments. For example, the storage device 140 may be a data storage device comprising a cloud computing platform, such as a public cloud, a private cloud, a community cloud, a hybrid cloud, and the like. However, such changes and modifications do not depart from the scope of the present application.
It should be understood that the system and its modules shown in FIG. 1 may be implemented in a variety of ways. It should be noted that the above description of the application scenario 100 is merely for convenience of description and is not intended to limit the present specification to the scope of the illustrated embodiments.
FIG. 2 is a schematic diagram of a system architecture for a biological growth system, according to some embodiments of the present disclosure.
As shown in fig. 2, a biological growth system may include a target gas enrichment module 1, a separation module 2, and a biological growth module.
The target gas enrichment module 1 can be used to obtain a mixed gas. Wherein the target gas is a gas required by the growth of the cultivated plants or microalgae. In some embodiments, the target gas may be carbon dioxide, nitrogen, oxygen, or the like. In some embodiments, the plant may include angiosperms (e.g., roses, pears, cherries, etc.), gymnosperms (e.g., pines, cypresses, maidenhair, torreya, yew, etc.), bryophytes (e.g., cucurbits, dictyophora, liverwort, griseum, dictamnus, rhodobryum, dictyophora, dictamnus, etc.), ferns (Ceratopteris viflora, Adenophora tetraphylla, Ceratopteris viflora, etc.), and the like that may be artificially cultivated. Algae may include green algae (chlorella, scenedesmus, oocystis, fibrophyceae, onchocerca, gossypium hirsutum, cladophora, etc.); diatoms (Cyclotella, Phoenix, Cyanophyta, Botrytis, etc.); blue-green algae (microcystis, anabaena, cyanobacteria, Oscillatoria, Schizochytrium, Spirulina, etc.); euglena (Euglena viridis, Euglena capsulata, Euglena fusca, etc.); dinoflagellates (gymnodinium, dinoflagellate, etc.); yellow algae (Bothrina, etc.); cryptophyceae (cryptophyceae, etc.); golden algae (small golden trichlorfon, golden pennycress, clockweed, Pandalus xanthioides, etc.) can be artificially cultured. The mixed gas is a gas containing a target gas. In some embodiments, the mixed gas may be a gas comprising the extraction species and the target gas. Wherein the extraction substance is a substance for extracting the target gas. For example, when the target gas is carbon dioxide, the extraction material may include one or more of alcohols (e.g., methanol, ethanol, propanol, 2-methyl-2-propanol), hydrocarbons (e.g., n-pentane), fluorinated hydrocarbons, ketones, esters, ethers, and siloxanes. The mixed gas is a gas comprising carbon dioxide and one or more of alcohols, hydrocarbons, fluorinated hydrocarbons, ketones, esters, ethers, siloxanes.
In some embodiments, the mixed gas may be obtained using an extraction substance based on the target gas enrichment module 1. The details are as follows.
The target gas enrichment module 1 may include a target gas selective permeation material, wherein the target gas selective permeation material is a single pass material, and the target gas enrichment module 1 may be divided into a high concentration unit and a low concentration unit using the target gas selective permeation material. Feeding an original gas from a low-concentration unit, and obtaining a first target gas in a high-concentration unit through a target gas selective permeation material; based on the first target gas, an extraction substance is added to the high concentration unit, and a mixed gas can be obtained. Wherein, the target gas selection material is a single-pass material which can pass through the target gas. For example, the target gas is carbon dioxide, and the target gas selective permeation material may be one or more of microporous alumina, microporous carbon, microporous silica, microporous perovskite, zeolite, and hydrotalcite.
In some embodiments, the raw gas, for example, air, is introduced into the low concentration unit of the target gas enrichment module 1, other gases in the air are filtered under the action of the target gas selective permeation material, carbon dioxide enters the high concentration unit from the low concentration unit to obtain a first target gas, and the concentration of carbon dioxide in the high concentration unit is increased under the action of the extraction substance, so as to obtain a mixed gas mixed with the extraction substance and carbon dioxide.
The separation module 2 is used for separating the mixed gas to obtain the target gas. As can be seen from the above, when the target gas is carbon dioxide, a mixed gas in which carbon dioxide and an extraction substance are mixed is obtained by the target gas enrichment module 1, and the extraction substance may be alcohols, for example: methanol, ethanol, propanol, 2-methyl-2-propanol, and the like. Depending on the nature of the extraction substance, a condenser may be used to separate the target gas and the extraction substance. Under the action of the condenser, the extraction substance is gradually liquefied along with the temperature reduction, carbon dioxide gas is discharged, and the liquefied extraction substance is gradually gasified after leaving the separator and returns to the target gas enrichment module 1 to form a circulation. In some embodiments, the separation module 2 may also include a still and a compressor.
Transmitting the target gas to the biological culture module according to a preset concentration threshold. The preset concentration threshold value can be set manually or obtained by counting historical data. In some embodiments, the preset concentration threshold may be a threshold interval or a single value. In some embodiments, the target gas meeting the concentration threshold interval may be transmitted to the biological culture module, the target gas greater than the maximum value of the concentration threshold interval may be mixed with air and then transmitted to the biological culture module, or the target gas less than the minimum value of the concentration threshold interval may be enriched and separated again and then transmitted to the biological culture module. For more description of the biological culture module, reference may be made to fig. 3, fig. 4 and the related description thereof, which are not repeated herein.
FIG. 3 is a schematic diagram of the connection of the first culture unit 3 according to some embodiments of the present disclosure.
As shown in fig. 3, the biological growth module may include a plurality of first growth units 3.
In some embodiments, the biological growth module comprises a plurality of first growth units 3, said first growth units 3 being connected in series by a main conduit from high to low according to a preset concentration threshold, and the output of the separation module 2 is connected to the input of each first growth unit 3 by a bypass conduit. As shown in fig. 3, in some embodiments, the output end of the separation module 2 and the output end of each first culture unit 3 are provided with a target gas concentration detection device 4, and the target gas concentration detection device 4 is used for detecting the target gas concentration output by the corresponding output end. For example, the target gas concentration detection device 4 is a carbon dioxide detection device that detects the concentration of carbon dioxide gas output from the corresponding output terminal. As shown in fig. 3, in some embodiments, a switching device 5 is provided on the main pipe at the input end of each first culturing unit 3; on the bypass pipeline, a switch device 5 is arranged at the joint of the input end of each first culture unit 3 and the bypass pipeline. The delivery of the target gas to each of the first culturing units 3 can be controlled by jointly controlling the switching devices 5 on the bypass line and the main line.
FIG. 4 is a schematic diagram of the connection of a second culture unit 6 according to some embodiments of the present disclosure.
In some embodiments, the biological growth module may further comprise a plurality of second growth units 6, at least one second growth unit 6 being connected in parallel to one first growth unit 3. As shown in FIG. 4, the number of the second culture units 6 may be the same as or different from the corresponding number of the first culture units 3.
As shown in FIG. 4, in some embodiments, the input of the second culturing unit 6 is provided with a switching device 5 for controlling the delivery of the target gas. The output end of the second culture unit 6 is also provided with a target gas concentration detection device 4 for detecting the target gas concentration output by the corresponding output end.
In some embodiments, the target gas may be delivered to the biological growth module according to a preset concentration threshold.
In some embodiments, delivering the target gas to the biological growth module includes the following steps.
Step 1: judging whether the input target gas concentration value belongs to a target gas concentration interval of the current first culture unit 3, if so, executing the step 2, if so, executing the step 3, and if not, judging the next stage and executing the step 1, wherein the maximum value of the target gas concentration interval of the current first culture unit 3 is larger than the maximum value of the target gas concentration interval of the current first culture unit 3; step 2: inputting the target gas to the current first culture unit 3; and step 3: and returning to the previous stage and executing the step 1. Further comprising: and 4, step 4: judging whether the input target gas concentration value belongs to a target gas concentration interval of the first-stage first culture unit 3, if so, executing the step 5, if so, executing the step 6, and if not, returning to the enrichment module and executing the step 4; and 5: inputting the target gas to the first-stage first culture unit 3; step 6: after the air is introduced, step 4 is performed. In some embodiments, the first culture unit 3 is connected in parallel with the second culture unit 6, and the above steps are also applicable to the second culture unit 6, and are not described herein.
Taking the target gas as carbon dioxide as an example, after high-concentration carbon dioxide is output from the separation module 2, the carbon dioxide sensor reads the concentration of the currently output carbon dioxide in real time, the system analyzes the output concentration, and if the concentration is in the concentration interval of the first-stage culture unit (including the first culture unit 3 and/or the corresponding second culture unit 6), the switch device 5 is controlled to feed the output carbon dioxide gas into the first-stage culture unit. When the concentration is higher than the upper limit of the concentration interval of the first-stage culture unit, the carbon dioxide gas is conveyed from the bypass to the input port of the first-stage culture unit through the change-over switch device 5 and then is judged, and if the carbon dioxide gas is in the concentration interval of the first-stage culture unit, the carbon dioxide gas is conveyed to the input port of the first-stage culture unit and is absorbed again. If the concentration is less than the concentration interval of the primary culture unit, returning to the target gas enrichment module 1, increasing the concentration of the target gas through the target gas enrichment module 1 and the separation module 2 again, judging, and repeating the above operations. In some embodiments, it is determined whether the current carbon dioxide concentration value belongs to a target gas concentration interval of the current culturing unit (the first culturing unit 3 and/or the corresponding second culturing unit 6), and if so, the carbon dioxide gas is input to the current culturing unit; if the concentration interval is larger than the maximum value of the concentration interval of the current culture unit, returning to the previous culture unit, judging the previous culture unit, and if the concentration interval is smaller than the minimum value of the concentration interval of the current culture unit, judging the next culture unit and repeating the operation. The target gas is transmitted to different culture units through different concentrations, so that the target gas is fully utilized, the utilization rate of the target gas is improved, and the loss is reduced.
It should be noted that the above description of a biological culture system is intended for purposes of illustration and description only and is not intended to limit the scope of applicability of the present description. Various modifications and alterations to the biological culture system will be apparent to those skilled in the art in light of this description. However, such modifications and variations are intended to be within the scope of the present description.
Having thus described the basic concept, it will be apparent to those skilled in the art that the foregoing detailed disclosure is to be regarded as illustrative only and not as limiting the present specification. Various modifications, improvements and adaptations to the present description may occur to those skilled in the art, although not explicitly described herein. Such modifications, improvements and adaptations are proposed in the present specification and thus fall within the spirit and scope of the exemplary embodiments of the present specification.
Also, the description uses specific words to describe embodiments of the description. Reference throughout this specification to "one embodiment," "an embodiment," and/or "some embodiments" means that a particular feature, structure, or characteristic described in connection with at least one embodiment of the specification is included. Therefore, it is emphasized and should be appreciated that two or more references to "an embodiment" or "one embodiment" or "an alternative embodiment" in various places throughout this specification are not necessarily all referring to the same embodiment. Furthermore, certain features, structures, or characteristics may be combined as suitable in one or more embodiments of the specification.
Additionally, the order in which the elements and sequences of the process are recited in the specification, the use of alphanumeric characters, or other designations, is not intended to limit the order in which the processes and methods of the specification occur, unless otherwise specified in the claims. While various presently contemplated embodiments of the invention have been discussed in the foregoing disclosure by way of example, it is to be understood that such detail is solely for that purpose and that the appended claims are not limited to the disclosed embodiments, but, on the contrary, are intended to cover all modifications and equivalent arrangements that are within the spirit and scope of the embodiments herein. For example, although the system components described above may be implemented by hardware devices, they may also be implemented by software-only solutions, such as installing the described system on an existing server or mobile device.
Similarly, it should be noted that in the preceding description of embodiments of the present specification, various features are sometimes grouped together in a single embodiment, figure, or description thereof for the purpose of streamlining the disclosure aiding in the understanding of one or more of the embodiments. This method of disclosure, however, is not intended to imply that more features than are expressly recited in a claim. Indeed, the embodiments may be characterized as having less than all of the features of a single embodiment disclosed above.
For each patent, patent application publication, and other material, such as articles, books, specifications, publications, documents, etc., cited in this specification, the entire contents of each are hereby incorporated by reference into this specification. Except where the application history document does not conform to or conflict with the contents of the present specification, it is to be understood that the application history document, as used herein in the present specification or appended claims, is intended to define the broadest scope of the present specification (whether presently or later in the specification) rather than the broadest scope of the present specification. It is to be understood that the descriptions, definitions and/or uses of terms in the accompanying materials of this specification shall control if they are inconsistent or contrary to the descriptions and/or uses of terms in this specification.

Claims (10)

1. A biological culture system is characterized by comprising a target gas enrichment module, a separation module and a biological culture module which are sequentially connected;
the target gas enrichment module is used for obtaining mixed gas;
the separation module is used for separating the mixed gas to obtain a target gas;
and transmitting the target gas to the biological culture module according to a preset concentration threshold value.
2. The biological cultivation system of claim 1 wherein the biological cultivation module includes a plurality of first cultivation units connected in series from high to low through a main conduit according to the preset concentration threshold, and the output of the separation module is connected to the input of each of the first cultivation units through a bypass conduit.
3. The biological growth system of claim 2 further comprising a plurality of second growth units, at least one of the second growth units being connected in parallel to one of the first growth units.
4. The biological cultivation system according to claim 3 wherein the output of the separation module and the output of each of the first cultivation unit and the second cultivation unit are provided with a target gas concentration detection device for detecting the target gas concentration output by the corresponding output.
5. The biological cultivation system of any one of claims 2 to 4 wherein delivering the target gas to the biological cultivation module according to a preset concentration threshold comprises:
step 1: judging whether the input target gas concentration value belongs to a target gas concentration interval of the current first culture unit, if so, executing the step 2, if so, executing the step 3, and if not, judging the next stage and executing the step 1;
step 2: inputting the target gas to a current first culture unit;
and step 3: and returning to the previous stage and executing the step 1.
6. The biological cultivation system of any one of claims 2 to 4 wherein delivering the target gas to the biological cultivation module according to a preset concentration threshold further comprises:
and 4, step 4: judging whether the input target gas concentration value belongs to a target gas concentration interval of the first-stage first culture unit, if so, executing the step 5, if so, executing the step 6, and if not, returning to the enrichment module and executing the step 4;
and 5: inputting the target gas to a first-stage first culture unit;
and 6: after the air is introduced, step 4 is performed.
7. The biological cultivation system according to any one of claims 1 to 4, wherein the target gas enrichment module for obtaining the mixed gas specifically comprises:
the target gas enrichment module comprises a target gas selective permeation material;
the target gas selective permeation material is a single-pass material, and the target gas enrichment module is divided into a high-concentration unit and a low-concentration unit;
raw gas is fed from the low concentration unit, and first target gas is obtained in the high concentration unit through the target gas selective permeation material;
and adding an extraction substance into the high-concentration unit based on the first target gas to obtain a mixed gas.
8. The biological cultivation system of claim 7 wherein the target gas selectively permeable material comprises: one or more of microporous alumina, microporous carbon, microporous silica, microporous perovskite, zeolite, and hydrotalcite.
9. A biological cultivation system as claimed in any one of claims 1 to 4 wherein the target gas is carbon dioxide.
10. The biological cultivation system of any one of claims 1 to 4 wherein the separation module includes one or more of a condenser, a distiller, a compressor.
CN202210781214.1A 2022-07-05 2022-07-05 Biological culture system Pending CN114854542A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106701574A (en) * 2016-12-31 2017-05-24 宁波华仪宁创智能科技有限公司 Cell culture operation integrated system and working method thereof
CN109810900A (en) * 2019-03-12 2019-05-28 华道(上海)生物医药有限公司 Totally-enclosed cell culture gas control system
CN110669667A (en) * 2019-09-27 2020-01-10 深圳先进技术研究院 Oxygen concentration controllable multi-channel culture system
CN113813774A (en) * 2021-08-27 2021-12-21 国家电投集团科学技术研究院有限公司 Carbon capture-algae/plant culture carbon fixation system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106701574A (en) * 2016-12-31 2017-05-24 宁波华仪宁创智能科技有限公司 Cell culture operation integrated system and working method thereof
CN109810900A (en) * 2019-03-12 2019-05-28 华道(上海)生物医药有限公司 Totally-enclosed cell culture gas control system
CN110669667A (en) * 2019-09-27 2020-01-10 深圳先进技术研究院 Oxygen concentration controllable multi-channel culture system
CN113813774A (en) * 2021-08-27 2021-12-21 国家电投集团科学技术研究院有限公司 Carbon capture-algae/plant culture carbon fixation system

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Application publication date: 20220805