CN113897272A - Filtration and sterilization device for supplementing inducer in glucosamine fermentation process and its application - Google Patents
Filtration and sterilization device for supplementing inducer in glucosamine fermentation process and its application Download PDFInfo
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- CN113897272A CN113897272A CN202111129220.0A CN202111129220A CN113897272A CN 113897272 A CN113897272 A CN 113897272A CN 202111129220 A CN202111129220 A CN 202111129220A CN 113897272 A CN113897272 A CN 113897272A
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- 238000000855 fermentation Methods 0.000 title claims abstract description 83
- 230000004151 fermentation Effects 0.000 title claims abstract description 83
- 239000000411 inducer Substances 0.000 title claims abstract description 50
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 44
- 230000001502 supplementing effect Effects 0.000 title claims abstract description 28
- MSWZFWKMSRAUBD-IVMDWMLBSA-N 2-amino-2-deoxy-D-glucopyranose Chemical compound N[C@H]1C(O)O[C@H](CO)[C@@H](O)[C@@H]1O MSWZFWKMSRAUBD-IVMDWMLBSA-N 0.000 title claims abstract description 24
- MSWZFWKMSRAUBD-UHFFFAOYSA-N beta-D-galactosamine Natural products NC1C(O)OC(CO)C(O)C1O MSWZFWKMSRAUBD-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 229960002442 glucosamine Drugs 0.000 title claims abstract description 24
- 238000001914 filtration Methods 0.000 title claims abstract description 18
- 238000004659 sterilization and disinfection Methods 0.000 title claims description 39
- BPHPUYQFMNQIOC-NXRLNHOXSA-N isopropyl beta-D-thiogalactopyranoside Chemical compound CC(C)S[C@@H]1O[C@H](CO)[C@H](O)[C@H](O)[C@H]1O BPHPUYQFMNQIOC-NXRLNHOXSA-N 0.000 claims abstract description 53
- 238000000034 method Methods 0.000 claims description 15
- 241000894006 Bacteria Species 0.000 claims description 7
- 238000004090 dissolution Methods 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000001963 growth medium Substances 0.000 claims description 2
- 239000008223 sterile water Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000011109 contamination Methods 0.000 abstract description 6
- 230000006698 induction Effects 0.000 abstract description 4
- 239000000654 additive Substances 0.000 description 6
- 238000011081 inoculation Methods 0.000 description 6
- 239000013589 supplement Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000006052 feed supplement Substances 0.000 description 3
- 230000009469 supplementation Effects 0.000 description 3
- QENJLXATANVWMR-UHFFFAOYSA-N 2-[(3-amino-3-imino-2-methylpropanethioyl)amino]acetic acid Chemical compound NC(=N)C(C)C(=S)NCC(O)=O QENJLXATANVWMR-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- 230000003321 amplification Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000003199 nucleic acid amplification method Methods 0.000 description 2
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 1
- 244000063299 Bacillus subtilis Species 0.000 description 1
- 235000014469 Bacillus subtilis Nutrition 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000011146 sterile filtration Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/04—Filters; Permeable or porous membranes or plates, e.g. dialysis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/12—Devices for taking out of action one or more units of multi- unit filters, e.g. for regeneration
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M37/00—Means for sterilizing, maintaining sterile conditions or avoiding chemical or biological contamination
- C12M37/02—Filters
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Abstract
The invention discloses a filtering and sterilizing device for supplementing an inducer in a glucosamine fermentation process and application thereof. Comprises a filter tank, wherein an air filter is longitudinally arranged in the middle of the filter tank; the bottom of the filter tank is provided with an exhaust and drainage valve; one end of the filter tank is connected with the material supplementing container through a first pipeline, and the other end of the filter tank is connected with the fermentation tank through a second pipeline; a first valve is arranged on the first pipeline; the second pipeline is provided with a steam inlet and is connected with the steam pipeline through the steam inlet; the second pipeline is also provided with a second valve and a third valve respectively; the second valve is located between the filter tank and the steam inlet, and the third valve is located between the steam inlet and the fermentation tank. The invention sterilizes the filter tank by external steam, does not need to be sterilized separately before adding IPTG, does not need to add IPTG in a sterile environment during fermentation, provides convenience for fermentation induction and production efficiency, greatly reduces operation steps and contamination probability, and has strong practicability.
Description
Technical Field
The invention relates to the technical field of fermentation, in particular to a filtering and sterilizing device and application thereof in supplementing an inducer in a glucosamine fermentation process.
Background
Glucosamine is mainly fermented by microorganisms, and production strains comprise microbial strains such as genetically engineered escherichia coli, bacillus subtilis and the like, however, in the fermentation process of genetically engineered bacteria, an inducer such as ITPG is usually added in the fermentation process, so that the products required by the induced expression of the engineered bacteria are started. However, many additives in the fermentation process cannot be sterilized at high temperature, such as inducer ITPG, lactose and the like, and once the additives are sterilized at high temperature, the induction fails in the fermentation process, and the fermentation fails, so that the inducer needs to be sterilized by filtration before being used in the glucosamine-induced fermentation process. In the process of fermenting and producing most microorganisms, materials need to be supplemented, particularly, inducers such as IPTG (isopropyl-beta-thiogalactoside) need to be supplemented in microbial fermentation of genetically engineered bacteria, the additives are extremely important to fermentation, but the supplementation amount is small, for example, in the process of supplementing IPTG, IPTG is dissolved in a sterile room and then is subjected to sterile filtration operation, then the IPTG is taken out of the sterile room in a sterile sealing mode, and then the IPTG is supplemented into a fermentation tank in a flame inoculation mode, so that the operation has large risk of bacterial contamination, complex operation and low efficiency, and often needs to be operated by multiple persons in a matching mode.
Therefore, a filtration and sterilization device for supplementing an inducer in the glucosamine fermentation process is needed, so that the manual filtration time of a fermentation workshop in a sterile room can be greatly saved, the chance of contamination is greatly reduced, the smooth fermentation is ensured, and the production efficiency is improved.
Disclosure of Invention
In view of the prior art, the invention aims to provide a filtration sterilization device for supplementing an inducer in a glucosamine fermentation process and application thereof. The invention sterilizes the filter tank by external steam, avoids conflict in material supplementing time or inaccurate control of the material supplementing time, and influences the fermentation production efficiency. The sterilization operation is not required to be carried out before the IPTG is added, the operation environment is not required, the IPTG is not required to be added in the sterile environment, convenience is provided for fermentation induction and production efficiency, the operation steps and the contamination probability are greatly reduced, and the practicability is high.
In order to achieve the purpose, the invention adopts the following technical scheme:
the invention provides a filtration and sterilization device for supplementing an inducer in a glucosamine fermentation process, which comprises a filter tank, wherein an air filter is longitudinally arranged in the middle of the filter tank; the bottom of the filter tank is provided with an exhaust and drainage valve; one end of the filter tank is connected with the material supplementing container through a first pipeline, and the other end of the filter tank is connected with the fermentation tank through a second pipeline; a first valve is arranged on the first pipeline; the second pipeline is provided with a steam inlet and is connected with the steam pipeline through the steam inlet; the second pipeline is also provided with a second valve and a third valve respectively; the second valve is located between the filter tank and the steam inlet, and the third valve is located between the steam inlet and the fermentation tank.
Preferably, the exhaust and drain valve is located at one end of the filter tank close to the first pipeline.
Preferably, the top of the feed supplement container is respectively provided with a pressure gauge and an air inlet pipe.
Preferably, the first pipeline and the second pipeline are respectively movably connected with two ends of the filter tank through threads.
Preferably, the lower part of the filter tank is provided with a movable bracket. The filter tank can be detached and moved, and is sterilized when a plurality of fermentation tanks are supplemented with the inducer.
Preferably, the first valve is located below the feed vessel.
Preferably, the second pipe extends deep inside the fermenter.
The device of the invention can also be provided with a plurality of filter tanks side by side, namely a plurality of parallel filter tanks are arranged between the material supplementing container and the fermentation tank, each filter tank is connected with the material supplementing container and the fermentation tank through an independent pipeline and is disinfected through an independent steam pipeline, and the specific arrangement is the same as that of the invention. By arranging the parallel filter tanks, when an inducer is added into one filter tank, other filter tanks can be sterilized; the alternative use of the filter tanks is realized.
In a second aspect of the invention, there is provided the use of a filter sterilization unit for supplementing an inducer.
In a third aspect of the present invention, there is provided a method for supplementing an inducer to a filter sterilization apparatus, comprising the steps of:
(1) steam sterilization: introducing steam into the steam pipeline, opening the first valve, the second valve, the third valve and the exhaust and drainage valve, and sterilizing the first pipeline, the second pipeline, the fermentation tank and the feeding container through the steam; closing the steam after the sterilization is finished, closing the first valve, the second valve, the third valve and the exhaust and drainage valve at the same time, and cooling for later use;
(2) preparation of IPTG inducer: adding the IPTG into a supplementing container, adding room-temperature sterile water to dissolve the IPTG, and simultaneously filling sterile air to accelerate the dissolution of the IPTG; after the IPTG is completely dissolved, an IPTG solution is obtained, a first valve is opened, the IPTG solution sequentially enters a first pipeline and a filter tank through the first valve, and is filtered and sterilized in the filter tank; opening a second valve, and allowing the IPTG solution after sterilization to enter a second pipeline;
(3) and (3) adding IPTG in the fermentation process: inoculating the culture medium into a fermentation tank, inoculating glucosamine bacteria, and culturing to obtain fermentation liquid OD600nmStarting to supplement IPTG solution with a value of 20-30; when the pressure in the feeding container is higher than the pressure in the fermentation tank, the third valve is opened, and IPTG is dissolved and enters the fermentation tank to complete the addition of the inducer.
Preferably, the sterilization time is 15-40 min;
preferably, the addition amount of the IPTG solution is 0.1-0.5 mmol/L of the volume of the fermentation broth.
The invention has the beneficial effects that:
the invention sterilizes the filter tank by external steam, thus solving the problem of aseptic addition of additives which can not be sterilized in the fermentation process. The inducer does not need to be sterilized independently before being added, the operating environment for fermentation does not need to be required, IPTG does not need to be added in the sterile environment, convenience is provided for fermentation induction and production efficiency, the operating steps and the contamination probability are greatly reduced, and the practicability is high. The device can be used for the sterile treatment of adding supplements like IPTG and the like, and the efficiency of the fermentation process is improved.
Drawings
FIG. 1: the structure schematic diagram of the filtration sterilization device for supplementing the inducer in the glucosamine fermentation process is disclosed;
wherein: 1. the system comprises a filter tank, 2 an air filter, 3 a feed supplement container, 4 a fermentation tank, 5 a first pipeline, 6 a second pipeline, 7 a steam inlet, 8 a steam pipeline, 9 a first valve, 10 a second valve, 11 a third valve, 12 an exhaust and drainage valve, 13 a movable support, 14 a pressure gauge and 15 an air inlet pipe.
Detailed Description
It should be noted that the following detailed description is exemplary and is intended to provide further explanation of the disclosure. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs.
In order to make the technical solutions of the present application more clearly understood by those skilled in the art, the technical solutions of the present application will be described in detail below with reference to specific embodiments.
The test materials used in the examples of the present invention are all conventional in the art and commercially available.
As described in the background art, in the existing glucosamine fermentation technology, because the used inducer cannot be sterilized at high temperature for sterilization, the inducer needs to be sterilized in a sterile workshop and then added into a fermentation tank. Because the fermentation cylinder height generally is between 10 ~ 20m, it is comparatively difficult to make the sterile chamber of such volume, moreover, in the fermentation production process, the addition of inducer is generally less, and long pipeline transport can lead to expensive inducer to remain in the pipeline, causes the loss to long pipeline transport also can greatly increased the risk of contracting a fungus. Therefore, the inducer cannot be supplemented into the fermentation tank in an aseptic environment, and the inducer is inevitably contaminated again by bacteria in the process of supplementing the inducer and the process of manually feeding and discharging the inducer into and out of the aseptic chamber for sterilization. Based on the above, the invention provides a filtration sterilization device for supplementing the inducer in the glucosamine fermentation process and application thereof. The filter tank is detachable, movable and can be installed in parallel, and the filter tank can be conveniently used among fermentation tanks. The device is suitable for the sterilization treatment of all fermentation additives which cannot be sterilized by high-temperature steam, and the fermentation efficiency is improved.
In the invention, the preparation and fermentation process control of the glucosamine bacteria are as follows:
(1) seed preparation: the producing strain is picked from the slant (or flat plate) of the mother strain to the shake flask.
(2) And (3) controlling a glucosamine fermentation process: inoculating the mixture into a 500L seed tank for amplification culture, further performing amplification culture in a 6-10 ton secondary seed tank, and performing 80-100M3And (4) fermentation culture, wherein sugar and IPTG inducer are supplemented in the fermentation process. IPTG inducer addition adopts the filtration sterilization device of the invention.
The following examples further illustrate the apparatus and applications of the present invention, and reference is made to the apparatus of the present invention for other fermentation processes that require additives that cannot be autoclaved.
Example 1
A filtration sterilization device for supplementing an inducer in a glucosamine fermentation process comprises a filter tank 1, wherein an air filter 2 is longitudinally arranged in the middle of the filter tank 1, as shown in figure 1; the bottom of the filter tank 1 is provided with an exhaust and drainage valve 12; one end of the filter tank 1 is connected with the material supplementing container 3 through a first pipeline 5, and the other end of the filter tank 1 is connected with the fermentation tank 4 through a second pipeline 6; a first valve 9 is arranged on the first pipeline 5; a steam inlet 7 is arranged on the second pipeline 6, and the second pipeline 6 is connected with a steam pipeline 8 through the steam inlet 7; a second valve 10 and a third valve 11 are respectively arranged on the second pipeline 6; the second valve 10 is located between the filter tank 1 and the steam inlet 7, and the third valve 11 is located between the steam inlet 7 and the fermentation tank 4.
The exhaust drain valve 12 is located at one end of the canister 1 adjacent to the first pipe 5. The top of the feed supplement container 3 is respectively provided with a pressure gauge 14 and an air inlet pipe 15. The first pipeline 5 and the second pipeline 6 are respectively movably connected with two ends of the filter tank 1 through threads. The lower part of the filter tank 1 is provided with a movable bracket 13. The first valve 9 is located below the feed vessel 3. The second pipe 6 extends into the interior of the fermenter 4.
Example 2
Glucosamine was prepared using the apparatus of example 1:
monitoring the thallus concentration OD during the fermentation process of glucosamine600nmWhen the OD value is 20-30, the IPTG inducer is added at one time, and the specific application operation is as follows:
(1) before the OD600nm value of 20, the device is steam sterilized, the third valve is closed, the second valve is opened, the exhaust and drain valve and the first valve can be in a half-open state, and the whole sterilization system and pipelines are sterilized, wherein the feeding container is included. (2) Sterilizing for 20 min. (3) And after the sterilization is finished, closing the steam. And simultaneously closing the second valve and the first valve, closing the exhaust and drainage valve, and cooling for standby. (4) The IPTG supplement is added according to 0.25mmol/L of the mass volume of the fermentation liquor. (5) And (3) putting the weighed addition amount of IPTG into a supplementing container, adding warm boiled water to dissolve the IPTG, and simultaneously filling workshop to filter air to accelerate the dissolution of the IPTG. (6) And after IPTG is completely dissolved, increasing the pressure in the feed supplementing container to be higher than the pressure in the fermentation tank, opening a third valve, and allowing IPTG solution to enter the fermentation tank after the filtration tank sterilizes to complete addition of the inducer. (7) And (4) measuring the glucosamine content when the cans are finally placed.
The experimental data were obtained by measuring 3 consecutive batches of the apparatus of example 1 after use and using the traditional inducer addition method with the same fermentation process: the flame inoculation inducer method was used as a control and the results are shown in Table 1.
Note: the flame inoculation inducer method comprises the following steps:
the inducer filtered by the sterile filter in the sterile room is packaged by a sterile container, and the outlet of the sterile container is wrapped by a sterile cotton plug, so that the inducer is prevented from being polluted in the process of taking out the inducer from the sterile room.
The operation process is as follows: the positive pressure is guaranteed in the fermentation tank, the cotton ring (the outlet of the fermentation tank can be sleeved by the size of the ring) which is soaked with alcohol is used for igniting the alcohol tampon, the flame is burnt, an operator wears a mask, one operator wears fireproof gloves to open the inoculation port of the fermentation tank, the other operator opens the outlet of a sterile container by enabling the container port filled with the sterile inducer to be close to the flame, the inducer is poured into the fermentation tank quickly, the inoculation port of the fermentation tank is screwed down after pouring, the flame ring is taken off and then is extinguished, and the operation is finished.
TABLE 1 comparison of test results
From the data of the four-batch comparative test results in the embodiment 2, the device provided by the invention is safe to use and operate, has no concern of contamination, is safe and reliable, has higher fermentation content of glucosamine than that of the conventional supplementing mode, and particularly has obviously improved glucose conversion rate.
Example 3
Glucosamine was prepared using the apparatus of example 1:
monitoring the thallus concentration OD during the fermentation process of glucosamine600nmWhen the OD value is 20-30, the IPTG inducer is added at one time, and the specific application operation is as follows:
(1) at OD600nmBefore the value is 30, the device is subjected to steam sterilization, the third valve is closed, the second valve is opened, the exhaust and drainage valve and the first valve can be in a half-open state, and the whole sterilization system and the pipeline are sterilized, wherein the whole sterilization system comprises a feeding container. (2) Sterilizing for 40 min. (3) And after the sterilization is finished, closing the steam. And simultaneously closing the second valve and the second valve 3, closing the exhaust and drain valve, and cooling for standby. (4) The IPTG supplement is added according to 0.4mmol/L of the mass volume of the fermentation liquor. (5) And (3) putting the weighed addition amount of IPTG into a supplementing container, adding warm boiled water to dissolve the IPTG, and simultaneously filling workshop to filter air to accelerate the dissolution of the IPTG. (6) And after IPTG is completely dissolved, increasing the pressure in the feed supplementing container to be higher than the pressure in the fermentation tank, opening a third valve, and allowing IPTG solution to enter the fermentation tank after the filtration tank sterilizes to complete addition of the inducer. (7) And (4) measuring the glucosamine content when the cans are finally placed.
The experimental data were obtained by measuring 3 consecutive batches of the apparatus of example 1 after use and using the traditional inducer addition method with the same fermentation process: the flame inoculation inducer method (see example 1 for specific operating methods) was used as a control and the results are shown in Table 2.
TABLE 2 comparison of test results
Example 3 from the results of four comparative experiments, it can be seen that the final glucosamine fermentation content is higher than that of the conventional supplementation mode, especially the glucose conversion rate is obviously improved by using the device of the present invention for IPTG supplementation.
The above description is only a preferred embodiment of the present application and is not intended to limit the present application, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, improvement and the like made within the spirit and principle of the present application shall be included in the protection scope of the present application.
Claims (10)
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| CN209816134U (en) * | 2019-03-05 | 2019-12-20 | 滨州职业学院 | A fermenter feeding device |
| CN213680613U (en) * | 2020-07-23 | 2021-07-13 | 福建康鸿生物科技有限公司 | Methanol supplementing device for fermentation tank |
| CN215975779U (en) * | 2021-09-26 | 2022-03-08 | 山东润德生物科技有限公司 | Filter sterilization device for supplementing inducer in glucosamine fermentation process |
-
2021
- 2021-09-26 CN CN202111129220.0A patent/CN113897272A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DD290212A5 (en) * | 1988-07-28 | 1991-05-23 | Zi Fuer Mikrobiologie Und Experimentelle Therapie,De | PROCESS FOR PREPARING A GLUCOSE MINIMUM MEDIUM FOR ESCHERICHIA COLI MASS CULTURE FERMENTATION |
| CN203373336U (en) * | 2013-07-17 | 2014-01-01 | 南京朗恩生物科技有限公司 | Sterile feeding device for fermentation tanks |
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| CN209816134U (en) * | 2019-03-05 | 2019-12-20 | 滨州职业学院 | A fermenter feeding device |
| CN213680613U (en) * | 2020-07-23 | 2021-07-13 | 福建康鸿生物科技有限公司 | Methanol supplementing device for fermentation tank |
| CN215975779U (en) * | 2021-09-26 | 2022-03-08 | 山东润德生物科技有限公司 | Filter sterilization device for supplementing inducer in glucosamine fermentation process |
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