CN105543077B - Biological food surfactant microemulsion production fermentation cauldron - Google Patents

Biological food surfactant microemulsion production fermentation cauldron Download PDF

Info

Publication number
CN105543077B
CN105543077B CN201610017026.6A CN201610017026A CN105543077B CN 105543077 B CN105543077 B CN 105543077B CN 201610017026 A CN201610017026 A CN 201610017026A CN 105543077 B CN105543077 B CN 105543077B
Authority
CN
China
Prior art keywords
fermentation
fermentation cauldron
stripper
snorkel
distribution plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201610017026.6A
Other languages
Chinese (zh)
Other versions
CN105543077A (en
Inventor
程叶红
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhongke Kangyuan (Tangshan) Biotechnology Co., Ltd.
Original Assignee
Fuzhou Changle Stock Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuzhou Changle Stock Technology Co Ltd filed Critical Fuzhou Changle Stock Technology Co Ltd
Priority to CN201610017026.6A priority Critical patent/CN105543077B/en
Publication of CN105543077A publication Critical patent/CN105543077A/en
Application granted granted Critical
Publication of CN105543077B publication Critical patent/CN105543077B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • 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
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • 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
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • C12M27/04—Stirrer or mobile mixing elements with introduction of gas through the stirrer or mixing element
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/82—Combinations of dissimilar mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/82—Combinations of dissimilar mixers
    • B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
    • B01F33/8212—Combinations of dissimilar mixers with consecutive receptacles with moving and non-moving stirring devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/017—Mixtures of compounds
    • 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
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
    • 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
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • C12M27/08—Stirrer or mobile mixing elements with different stirrer shapes in one shaft or axis
    • 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
    • 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
    • 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
    • C12M29/08—Air lift
    • 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
    • C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • 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
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • 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
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
    • C12M41/24—Heat exchange systems, e.g. heat jackets or outer envelopes inside the vessel
    • 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
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/26—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pH
    • 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
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • 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
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • C12M43/02—Bioreactors or fermenters combined with devices for liquid fuel extraction; Biorefineries
    • 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
    • C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/10—Separation or concentration of fermentation products
    • 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
    • C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
    • C12M47/12—Purification
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/21—Mixing of ingredients for cosmetic or perfume compositions

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Biotechnology (AREA)
  • General Engineering & Computer Science (AREA)
  • Sustainable Development (AREA)
  • Biochemistry (AREA)
  • Microbiology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Biomedical Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Molecular Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Colloid Chemistry (AREA)

Abstract

The present invention relates to a kind of biological food surfactant microemulsion production fermentation cauldron, the fermentation cauldron for microbial fermentation production biosurfactant；The second rabbling mechanism is provided in fermentation cauldron, the top of fermentation cauldron is provided with material input port, discharge port is arranged in the lower part of fermentation cauldron, second rabbling mechanism includes the second agitating shaft of vertical shape arrangement, the periphery of second agitating shaft is uniformly arranged the snorkel of vertical shape arrangement, and gas distribution plate is arranged at intervals on the pipe shaft of snorkel.The biological surfactant microemulsion production of the fermentation cauldron provided in above-mentioned technical proposal, can quickly be made the micro emulsion of biosurfactant.

Description

Biological food surfactant microemulsion production fermentation cauldron
It is on November 14th, 2014 that the present invention, which is the applying date, application No. is 201410650537.2, entitled " makeup The divisional application of the patent of invention of the biological surfactant microemulsion production system of product, food, chemical industry and agricultural ".
Technical field
The present invention relates to emulsifier production fields, and in particular to a kind of cosmetics, food, chemical industry and agricultural are lived with biological table Agent microemulsion production system.
Background technology
Micro emulsion is the transparent or semitransparent thermodynamic stable system spontaneously formed, there is two kinds of oil-in-water and Water-In-Oil Type.The formation of micro emulsion is spontaneous, does not need extraneous offer energy, is a kind of system that thermodynamics is highly stable, because This is widely used in fields such as petrochemical industry, cosmetics, food.Wherein, the microemulsion prepared by biosurfactant Liquid is usually used in the cosmetics of super quality, more stable, safe, skin absorption is good.The preparation method of such micro emulsion is：It will Biosurfactant (Lipopeptide Biosurfactants), cosurfactant (C3~C5 alcohol) are mixed with alkali (sodium hydroxide) Forming surfactants mixed liquor is prepared, water phase (generally brine) is prepared, prepares oil phase (generally alkane, cycloalkane, fragrance Hydrocarbon)；Prepared surfactant mixed liquor is added in water phase and is uniformly mixed, then oil phase is instilled to above-mentioned solution dropwise In, and constantly stir evenly, until solution by muddiness to clarifying, obtain the micro emulsion being made of biosurfactant, Due to needing using oil phase is added dropwise dropwise, so that the throughput rate bottom of micro emulsion, seriously affects production rate.
Invention content
It is an object of the invention to provide a kind of biological food surfactant microemulsion production fermentation cauldrons.
To achieve the above object, present invention employs following technical schemes：
A kind of biological food surfactant microemulsion production fermentation cauldron, which is characterized in that including following production equipment:
The fermentation cauldron of biosurfactant is produced for microbial fermentation；
For in fermentation cauldron zymotic fluid carry out purifies and separates processing zymotic fluid purifier apparatus and for storing it is pure The biosurfactant storage tank of biosurfactant after change；
It is respectively used to cosurfactant storage tank, the lye storage of storage cosurfactant, lye, water phase and oil phase Tank, water phase storage tank and oil phase storage tank；
And surfactant Compound mixed solution kettle and micro emulsion reaction kettle；Fermentation cauldron, zymotic fluid purifier apparatus and life Object surfactant storage tank is attached successively, biosurfactant storage tank, cosurfactant storage tank and alkali liquor storage tank Liquid outlet be connected with surfactant Compound mixed solution kettle, surfactant Compound mixed solution kettle and water phase storage tank go out Liquid mouth is connected with micro emulsion reaction kettle；
The second rabbling mechanism is provided in fermentation cauldron, the top of fermentation cauldron is provided with material input port, the lower part of fermentation cauldron Discharge port is set, and the second rabbling mechanism includes the second agitating shaft of vertical shape arrangement, and the periphery of the second agitating shaft is uniformly arranged vertical shape The snorkel of arrangement is arranged at intervals with gas distribution plate on the pipe shaft of snorkel, offers in the middle part of each gas distribution plate and stirred for second Mix axis by through-hole, the inside of gas distribution plate is arranged to uniformly open up qi-emitting hole in the plate face of cavity-like and gas distribution plate, respectively Strainer is provided at qi-emitting hole, the tube chamber of each snorkel is connected with the inner cavity of a gas distribution plate respectively to be connect, each snorkel Upper end is connected after passing through fermentation cauldron autoclave body with air-blowing device, and temperature sensor and PH measurement assemblies are additionally provided in fermentation cauldron；
Shedding mechanism is provided at discharge port, shedding mechanism includes the circle being arranged in parallel above and below at fermentation tank discharge port The first and second stripper, the first stripper is fixed with one with fermentation tank, and annular groove is offered on the side of the second stripper, Second stripper is rotatably assorted around vertical direction composition with fermentation tank by the steel ball component being arranged in annular groove and is connect, first, The center of circle of two strippers is located on same plumb line, opens up on the first and second stripper at the circumference of same radius size respectively One, two discharge port, the lower face of the first stripper, which is arranged to be combined by the first and second step surface, constitutes step-like, second step Face and the upper face of the second stripper fit, and cavity is formed between First terrace and the second stripper upper face, and first unloads Material mouth is opened on First terrace, is provided with sealing element at the step that the first and second step surface is joined, the shape of sealing element and the One, the step shape of two step surface junctions is consistent, and the second stripper is connected with driving mechanism.
The biological surfactant microemulsion production system of cosmetics, food, chemical industry and agricultural provided in above-mentioned technical proposal, By carrying out purifying and microemulsified processing to zymotic fluid, to which the micro emulsion of biosurfactant quickly be made.
Description of the drawings
Fig. 1 is the structural diagram of the present invention；
Fig. 2 is the structural schematic diagram of zymotic fluid purifier apparatus；
Fig. 3 is the structural schematic diagram of the second rabbling mechanism, gas distribution plate and snorkel；
Fig. 4 is the structural schematic diagram of the first rabbling mechanism, liquid distribution plate part and oil phase inlet tube；
Fig. 5 is the structural schematic diagram of gas distribution plate；
Fig. 6 is the structural schematic diagram of liquid distribution plate part；
Fig. 7 is the structural schematic diagram of shedding mechanism；
Fig. 8 is the structural schematic diagram of plate face on the downside of the first stripper.
Specific implementation mode
In order to make objects and advantages of the present invention be more clearly understood, the present invention is carried out specifically with reference to embodiments It is bright.It should be appreciated that following word is only used to one or more of specific embodiments of the description present invention, not to the present invention The protection domain specifically asked carries out considered critical.
The technical solution that the present invention takes is as shown in Figure 1, 2, and a kind of cosmetics, food, chemical industry and agricultural are lived with biological table Agent microemulsion production system, which is characterized in that including following production equipment:
The fermentation cauldron 40 of biosurfactant is produced for microbial fermentation；
For carrying out the zymotic fluid purifier apparatus 90 of purifies and separates processing to the zymotic fluid in fermentation cauldron 40 and for storing up Put the biosurfactant storage tank 10 of biosurfactant after purification；
It is respectively used to cosurfactant storage tank 80, the lye storage of storage cosurfactant, lye, water phase and oil phase Tank 50, water phase storage tank 60 and oil phase storage tank 70；
And surfactant Compound mixed solution kettle 20 and micro emulsion reaction kettle 30；Fermentation cauldron, zymotic fluid purifier apparatus It is attached successively with biosurfactant storage tank, biosurfactant storage tank, cosurfactant storage tank and lye The liquid outlet of storage tank is connected with surfactant Compound mixed solution kettle, surfactant Compound mixed solution kettle and water phase storage tank Liquid outlet be connected with micro emulsion reaction kettle.
The biological surfactant microemulsion production system of cosmetics, food, chemical industry and agricultural provided in above-mentioned technical proposal, By carrying out purifying and microemulsified processing to zymotic fluid, to which the micro emulsion of biosurfactant quickly be made.Due to The period of fermentation is longer, and in order to ensure the continuity of production, multiple fermentation cauldrons, the zymotic fluid outlet of multiple fermentation cauldrons can be arranged It is connected respectively with purification devices.
Due to fermentation broth contents complexity, including thalline, the solid medium not being fermented, not by microorganism full utilization Carbohydrate, inorganic salts, protein and the various metabolites of microorganism, fermentation broth viscosity is big, for zymotic fluid purifier apparatus, It specifically can be as shown in Fig. 2, including latter linked dilution device 91, rough filtering device 92, micro-filtration 93, decontamination before setting gradually Albumen device 94, decontamination ion unit 95 and salinization device 96.Dilution device is mainly diluted and adjusts to zymotic fluid PH is generally constituted using groove body；Rough filtering device mainly by zymotic fluid thalline, the solid medium that is not fermented and other Spin-on filter device or other filter plants can be used to getting rid of in larger solid impurity, and multiple filterings can also be used and set Standby to be used in conjunction, the zymotic fluid after thick worry can be diluted and adjust again PH；Micro-filtration mainly removes the small molecular weight impurity in zymotic fluid, Such as pigment is generally carried out using film filter, and the aperture of used filter membrane should be according to purpose biosurfactant Molecular size chosen, should filter membrane retain biosurfactant, ceramic membrane generally can be used；Micro-filtration Later it can be diluted and adjust herein PH；Decontamination albumen device can be isoelectric precipitation device, decontamination ion unit Predominantly resin adsorption device, by being eluted to the MICROBIAL SURFACTANT after absorption, eluent is with lye in salinization Reaction is carried out in device generates salt.It can not certainly for purifier apparatus used by different types of biosurfactant Together, the specific purifier apparatus that this law provides is primarily adapted for use in the purification process of Lipopeptide Biosurfactants.For other The purifying of the biosurfactant (such as carbohydrate, lipoprotein) of type, substantially flow are also dilution, thick worry, micro-filtration, removal Impurity protein and ion.
Since fermentation broth viscosity is big in fermentation cauldron, conventionally employed tracheae is passed through air it is difficult to ensure that filtrated air is being sent out Being uniformly distributed in fermentation tank.Therefore, the present invention is implemented using the technical side as shown in Fig. 3,5：The be arranged in fermentation cauldron The top of two rabbling mechanisms, fermentation cauldron is provided with material input port, and discharge port, the second rabbling mechanism packet is arranged in the lower part of fermentation cauldron The second agitating shaft 41 of vertical shape arrangement is included, the periphery of the second agitating shaft 41 is uniformly arranged the snorkel 45 of vertical shape arrangement, snorkel Be arranged at intervals with gas distribution plate 46 on 45 pipe shaft, the middle part of each gas distribution plate 46 offer for the second agitating shaft 41 by it is logical Hole, the inside of gas distribution plate 46 are arranged to uniformly open up qi-emitting hole 461 in the plate face of cavity-like and gas distribution plate 46, each qi-emitting hole Strainer is provided at 461, the tube chamber of each snorkel is connected with the inner cavity of a gas distribution plate 46 respectively to be connect, each snorkel 45 Upper end is connected after passing through autoclave body with air-blowing device, and temperature sensor and PH measurement assemblies are additionally provided in fermentation cauldron.Stratiform is arranged The gas distribution plate 46 of cloth can supplement air so that air in zymotic fluid when blasting filtrated air from each layer phase zymotic fluid Uniformly, ensure the fermentation of biosurfactant.
Preferably scheme is：A cone-shaped hood that Open Side Down may be used and constitute gas distribution plate, opened up in the middle part of cone-shaped hood Through-hole is arranged to cavity-like inside the cover body of cone-shaped hood, qi-emitting hole 461 is uniformly arranged in the outer cover of cone-shaped hood.Such gas distribution Uniformity and horizontal covering surface it is maximum, as shown in Figure 5.There are three the gas distribution plate stratiform settings, snorkel setting There are three, the upper end of snorkel passes through four-pass connecting joint and tracheae and drum after the motor mount on fermentation cauldron autoclave body top Device of air is connected.
It is further as shown in Figure 7,8, shedding mechanism is provided at discharge port, shedding mechanism includes at fermentation tank discharge port Circular first and second stripper 42,43 being arranged in parallel above and below, the first stripper 42 are fixed with one with fermentation tank, and second unloads Offer annular groove on the side of flitch 43, the second stripper 43 by the steel ball component 48 that is arranged in annular groove and fermentation tank around Vertical direction constitutes the connection that is rotatably assorted, and the center of circle of the first and second stripper 42,43 is located on same plumb line, the first and second discharging Open up first and second discharge port 42a, 43a, the lower face setting of the first stripper 42 on plate at the circumference of same radius size respectively Step-like, the upper face in second step face 422 and the second stripper 43 is constituted at by the combination of the first and second step surface 421,422 It fits, forms cavity between 43 upper face of First terrace 421 and the second stripper, the first discharge port 42a is opened in first On step surface 421, sealing element 423, the shape of sealing element 423 and first and second are provided at the step that the first and second step surface is joined The step shape of step surface junction is consistent, and the second stripper 43 is connected with driving mechanism, and preferred scheme is：First and second The outer profile of step surface junction is arc, sets sealing element to arc in this way, and sealing element can be used O-ring seals, first The height that the upper face of stripper is arranged at taper and the first discharge port is minimum.By driving mechanism adjust the second stripper into Row rotation so that the first and second discharge port on the first and second stripper is corresponding and different, to realize to the quick of fermentation tank The closure of discharging and discharge port realizes quickly discharging material, to save the time, improves extraction efficiency.
In order to improve the rate of microemulsified, the present invention is implemented using the technical side as shown in Fig. 4,6：Micro emulsion is anti- It includes the first stirring of vertical shape arrangement to answer the first rabbling mechanism being arranged in kettle, including autoclave body and autoclave body, the first rabbling mechanism Axis 31, the periphery of the first agitating shaft 31 are uniformly arranged the oil phase inlet tube 35 of vertical shape arrangement, on the pipe shaft of oil phase inlet tube 35 between Every being provided with liquid distribution plate part 36, the middle part of each liquid distribution plate part 36 offer for the first agitating shaft 31 by through-hole, liquid distribution plate part 36 inside is arranged to cavity-like and the lower face of liquid distribution plate part 36 uniformly opens up liquid distributing hole, the tube chamber difference of each oil phase inlet tube It is connected with the inner cavity of a liquid distribution plate part 36 and connect, the upper end of each oil phase inlet tube is connected after autoclave body with oil phase storage tank, Surfactant mixed liquor feed liquor nozzle and water phase feed liquor nozzle are additionally provided on autoclave body.The liquid distribution plate part 36 of stratiform arrangement, When oil phase is added dropwise, oil phase is instilled from each liquid distributing hole on liquid distribution plate part 36 in the mixed liquor in reaction kettle, relative to traditional One after another drop of instillation significantly improves production efficiency.Certain spacing should be kept between each liquid distributing hole, when specific operation, liquid distributing hole is The needle tubing plugged on liquid distribution plate part 36 is constituted, and the length of adjacent needle tubing is different.
Preferably scheme is：Liquid distribution plate part 36 is that the cone-shaped hood of an opening upwards is constituted, and through-hole is opened up in the middle part of cone-shaped hood, It is arranged to cavity-like inside the cover body of cone-shaped hood, the needle tubing 361 for constituting qi-emitting hole is uniformly arranged in the outer cover of cone-shaped hood, The length direction of needle tubing 361 and the perpendicular arrangement of the cover of cone-shaped hood, needle tubing is arranged on the cover of cone-shaped hood in round, and needle The length of pipe increases with the radius of cone-shaped hood and is increased, and instills the best results of oil phase in this way.The liquid distribution plate part stratiform is set There are three setting, oil phase inlet tube is provided with three, and the upper end of oil phase inlet tube passes through four-pass connecting joint and material after autoclave body Liquid conveyance conduit is connected with oil phase storage tank.
Due to being respectively provided with distribution device and liquid distributor, the first and second agitating shaft axle body on the first and second agitating shaft On agitating paddle can not be set, therefore the first and second rabbling mechanism is implemented using identical technical solution in the present invention, Yi Jiru Fig. 3, shown in 4, the radial setting connecting rod in lower end of the first and second agitating shaft 31,41, the end of connecting rod is stood shape setting and is stirred respectively Bar is mixed, the agitating paddle 34 of stirring feed liquid is respectively set in connecting rod and/or stirring rod.The length for being specifically stirring rod is connection Twice of bar, connecting rod include the first, second and third connecting rod 324,322,323, stirring rod include the first, second and third stirring rod 334, 332,333, stirring is respectively set in the epimere of head rod 324, the hypomere of the second stirring rod 332 and third stirring rod 333 Paddle 34, agitating paddle 34 are that a plate is constituted, and such rabbling mechanism can from different directions be stirred solution, improve mixed The uniformity of conjunction.Stirring rod and connecting rod are that angle steel is constituted, and such intensity is big, the installation convenient for agitating paddle 34 and blender The stability of structure.
In addition, for fermentation cauldron, the kettle wall of fermentation cauldron is sandwich, and the clip cavity that sandwich is formed is for accommodating hot-fluid Body.Hot fluid meets the needs of microbial fermentation for adjusting fermentation temperature in the kettle.For micro emulsion reaction kettle, autoclave body Flow-interfering bar is provided on madial wall, the side wall of autoclave body is constituted for sandwich, and the clip cavity that sandwich is formed is for accommodating hot-fluid Body.Hot fluid adapts to the production of different micro emulsions for adjusting temperature in the kettle.
Third rabbling mechanism and ultrasound emission component, surfactant are provided in surfactant Compound mixed solution kettle The kettle wall for preparing kettle is sandwich, the clip cavity of sandwich formation for accommodating heating fluid.Ultrasound emission component is to material It is vibrated so that the quick mixing of surfactant, cosurfactant.
In short, the present invention can effectively improve the production efficiency of micro emulsion.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, after knowing content described in the present invention, without departing from the principle of the present invention, it can also be made several Same transformation and replacement, these convert and substitute on an equal basis and also should be regarded as belonging to the scope of protection of the present invention.

Claims (2)

1. a kind of biological food surfactant microemulsion production fermentation cauldron, which is characterized in that fermentation cauldron, zymotic fluid purifier apparatus and Biosurfactant storage tank is attached successively, and the second rabbling mechanism is provided in fermentation cauldron, and the top of fermentation cauldron is provided with Discharge port is arranged in the lower part of material input port, fermentation cauldron, and the second rabbling mechanism includes the second agitating shaft of vertical shape arrangement, and second stirs The periphery for mixing axis is uniformly arranged the snorkel of vertical shape arrangement, and gas distribution plate, each air distribution plate are arranged at intervals on the pipe shaft of snorkel Offered in the middle part of part for the second agitating shaft by through-hole, the inside of gas distribution plate is arranged to the plate of cavity-like and gas distribution plate Qi-emitting hole is uniformly opened up on face, is provided with strainer at each qi-emitting hole, the tube chamber of each snorkel inner cavity with a gas distribution plate respectively Be connected connection, and the upper end of each snorkel is connected after fermentation cauldron autoclave body with air-blowing device, and temperature is additionally provided in fermentation cauldron Spend sensor and PH measurement assemblies；
Shedding mechanism is provided at discharge port, shedding mechanism includes circular to be arranged in parallel above and below at fermentation tank discharge port One, two stripper, the first stripper are fixed with one with fermentation tank, offer annular groove on the side of the second stripper, and second Stripper is rotatably assorted around vertical direction composition with fermentation tank by the steel ball component being arranged in annular groove and is connect, and first and second unloads The center of circle of flitch is located on same plumb line, and first and second is opened up respectively at the circumference of same radius size on the first and second stripper Discharge port, the lower face of the first stripper, which is arranged to be combined by the first and second step surface, constitutes step-like, second step face and the The upper face of two strippers fits, and cavity is formed between First terrace and the second stripper upper face, and the first discharge port is opened It is located on First terrace, sealing element, the shape of sealing element and first and second is provided at the step that the first and second step surface is joined The step shape of step surface junction is consistent, and the second stripper is connected with driving mechanism.
2. biological food surfactant microemulsion production fermentation cauldron according to claim 1, it is characterised in that：The cloth There are three the settings of gas plate stratiform, and snorkel is provided with three, and the upper end of snorkel passes through the motor on fermentation cauldron autoclave body top to pacify It is connected with air-blowing device by four-pass connecting joint and tracheae after dress seat.
CN201610017026.6A 2014-11-14 2014-11-14 Biological food surfactant microemulsion production fermentation cauldron Active CN105543077B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610017026.6A CN105543077B (en) 2014-11-14 2014-11-14 Biological food surfactant microemulsion production fermentation cauldron

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201410650537.2A CN104450510B (en) 2014-11-14 2014-11-14 Cosmetics, food, chemical industry and agricultural biology surfactant microemulsion production system
CN201610017026.6A CN105543077B (en) 2014-11-14 2014-11-14 Biological food surfactant microemulsion production fermentation cauldron

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201410650537.2A Division CN104450510B (en) 2014-11-14 2014-11-14 Cosmetics, food, chemical industry and agricultural biology surfactant microemulsion production system

Publications (2)

Publication Number Publication Date
CN105543077A CN105543077A (en) 2016-05-04
CN105543077B true CN105543077B (en) 2018-10-16

Family

ID=52897269

Family Applications (12)

Application Number Title Priority Date Filing Date
CN201610017018.1A Active CN105543076B (en) 2014-11-14 2014-11-14 The biological surfactant microemulsion production system of food
CN201610017026.6A Active CN105543077B (en) 2014-11-14 2014-11-14 Biological food surfactant microemulsion production fermentation cauldron
CN201610017016.2A Active CN105543075B (en) 2014-11-14 2014-11-14 The biological surfactant microemulsion production system of agricultural
CN201610016980.3A Active CN105505757B (en) 2014-11-14 2014-11-14 A kind of biological surfactant microemulsion production system of chemical industry
CN201610014953.2A Active CN105420093B (en) 2014-11-14 2014-11-14 Biological surfactant microemulsion production system for cosmetics
CN201610017017.7A Active CN105482997B (en) 2014-11-14 2014-11-14 A kind of biology surfactant microemulsion production fermentation cauldron
CN201610016998.3A Expired - Fee Related CN105505758B (en) 2014-11-14 2014-11-14 Cosmetics biology surfactant microemulsion production fermentation cauldron
CN201610015551.4A Active CN105505748B (en) 2014-11-14 2014-11-14 A kind of biological surfactant microemulsion production system for chemical industry
CN201410650537.2A Active CN104450510B (en) 2014-11-14 2014-11-14 Cosmetics, food, chemical industry and agricultural biology surfactant microemulsion production system
CN201610015244.6A Active CN105420094B (en) 2014-11-14 2014-11-14 Biological surfactant microemulsion production system for food
CN201610017019.6A Expired - Fee Related CN105879816B (en) 2014-11-14 2014-11-14 Cosmetics biology surfactant microemulsion production micro emulsion reaction kettle
CN201610015251.6A Active CN105543074B (en) 2014-11-14 2014-11-14 A kind of fermentation cauldron for microbial fermentation production biosurfactant

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN201610017018.1A Active CN105543076B (en) 2014-11-14 2014-11-14 The biological surfactant microemulsion production system of food

Family Applications After (10)

Application Number Title Priority Date Filing Date
CN201610017016.2A Active CN105543075B (en) 2014-11-14 2014-11-14 The biological surfactant microemulsion production system of agricultural
CN201610016980.3A Active CN105505757B (en) 2014-11-14 2014-11-14 A kind of biological surfactant microemulsion production system of chemical industry
CN201610014953.2A Active CN105420093B (en) 2014-11-14 2014-11-14 Biological surfactant microemulsion production system for cosmetics
CN201610017017.7A Active CN105482997B (en) 2014-11-14 2014-11-14 A kind of biology surfactant microemulsion production fermentation cauldron
CN201610016998.3A Expired - Fee Related CN105505758B (en) 2014-11-14 2014-11-14 Cosmetics biology surfactant microemulsion production fermentation cauldron
CN201610015551.4A Active CN105505748B (en) 2014-11-14 2014-11-14 A kind of biological surfactant microemulsion production system for chemical industry
CN201410650537.2A Active CN104450510B (en) 2014-11-14 2014-11-14 Cosmetics, food, chemical industry and agricultural biology surfactant microemulsion production system
CN201610015244.6A Active CN105420094B (en) 2014-11-14 2014-11-14 Biological surfactant microemulsion production system for food
CN201610017019.6A Expired - Fee Related CN105879816B (en) 2014-11-14 2014-11-14 Cosmetics biology surfactant microemulsion production micro emulsion reaction kettle
CN201610015251.6A Active CN105543074B (en) 2014-11-14 2014-11-14 A kind of fermentation cauldron for microbial fermentation production biosurfactant

Country Status (1)

Country Link
CN (12) CN105543076B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3057743B1 (en) * 2016-10-21 2018-10-26 B2B Cosmetics MIXER SYSTEM FOR MANUFACTURING A COSMETIC PRODUCT AND COSMETIC CAPSULE
CN109351217B (en) * 2018-11-22 2022-06-17 然晟(上海)实业发展有限公司 Ultrasonic emulsification device for preparing pesticide microcapsules

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1410514A (en) * 2002-09-29 2003-04-16 季忠 Production technology and formulation of microemulsion fuel oil
CN1233447C (en) * 2003-12-24 2005-12-28 华东理工大学 Micro lactescence and its preparing method
CN1632067A (en) * 2004-11-19 2005-06-29 季忠 Method for producing microemulsified fuel oil
CN101086006B (en) * 2007-06-26 2011-02-09 湖南大学 Composite type biological surfactant and its production method
JP2011152992A (en) * 2010-01-27 2011-08-11 Enutekku:Kk Powder and grain quantitative discharging apparatus
CN101948737B (en) * 2010-08-31 2013-06-05 天津理工大学 Acetone-butanol in-situ extraction continuous fermentation device and technology
CN201840992U (en) * 2010-10-22 2011-05-25 安徽本雅明涂料有限公司 Combined agitating device
CN201949845U (en) * 2010-12-30 2011-08-31 荆州市江汉精细化工有限公司 Stirring device for reaction kettle
CN202075932U (en) * 2011-06-09 2011-12-14 淮南赛力威机电设备有限责任公司 Self-rescuer seal strip protector
CN202129072U (en) * 2011-06-12 2012-02-01 崔建 Reactor for producing resin products
CN202207593U (en) * 2011-08-01 2012-05-02 河南利伟生物药业股份有限公司 Oxidizing reaction kettle
CN102757994A (en) * 2011-09-21 2012-10-31 大庆沃太斯化工有限公司 Industrial production method of lipopeptide bio-surfactant
CN202460511U (en) * 2012-02-24 2012-10-03 福建省圣川节能服务有限公司 Stirring mechanism of beating machine
CN202705112U (en) * 2012-04-09 2013-01-30 江苏天目建设集团有限公司 Umbrella flow cutting type aerator
CN203090838U (en) * 2012-12-25 2013-07-31 河南工业职业技术学院 Anchor agitator with cutting function
CN203096077U (en) * 2013-02-21 2013-07-31 哈尔滨师范大学 Automatically controlled aerobic microorganism fermentation tank
CN203170328U (en) * 2013-05-03 2013-09-04 潍坊兴信技术服务有限公司 Reaction kettle
CN203469878U (en) * 2013-08-22 2014-03-12 福建省华普新材料有限公司 Material stirrer
CN203546018U (en) * 2013-10-12 2014-04-16 北京市捷博特能源技术有限公司 Low-temperature sterilization and waste liquor recovery device for fermentation ingredient liquor of lipopeptid surfactant
CN203530305U (en) * 2013-10-15 2014-04-09 陈烨 Ecological non-dead-corner aeration device
CN103627621B (en) * 2013-12-23 2016-01-20 齐鲁工业大学 Solid-state vertical type fermentation, self-circulation cooling, distillation integrated apparatus and method
CN203620638U (en) * 2014-01-03 2014-06-04 克拉玛依市金鑫科技有限公司 Microemulsion polymerization reaction kettle
CN203668396U (en) * 2014-01-09 2014-06-25 盐城师范学院 Simple bioreactor for fermentation production of surfactant by using seawater
CN203855592U (en) * 2014-04-09 2014-10-01 廊坊师范学院 Animal cell suspension culture flask
CN203842553U (en) * 2014-05-16 2014-09-24 浙江雨兰建材有限公司 Stirring device for dispersion machine

Also Published As

Publication number Publication date
CN105420093B (en) 2019-01-08
CN105543075A (en) 2016-05-04
CN105543074A (en) 2016-05-04
CN105543076A (en) 2016-05-04
CN105420093A (en) 2016-03-23
CN105482997B (en) 2018-08-31
CN105505758A (en) 2016-04-20
CN105505757A (en) 2016-04-20
CN105543076B (en) 2018-10-16
CN105505757B (en) 2018-11-02
CN105543074B (en) 2018-08-31
CN105420094B (en) 2018-08-31
CN105505758B (en) 2018-09-18
CN105505748A (en) 2016-04-20
CN105482997A (en) 2016-04-13
CN104450510B (en) 2016-06-08
CN105420094A (en) 2016-03-23
CN105505748B (en) 2018-08-31
CN105879816A (en) 2016-08-24
CN105543077A (en) 2016-05-04
CN105879816B (en) 2018-12-21
CN104450510A (en) 2015-03-25
CN105543075B (en) 2019-03-15

Similar Documents

Publication Publication Date Title
US4876013A (en) Small volume rotary filter
JPS61500716A (en) Filtration method and device
CN105543077B (en) Biological food surfactant microemulsion production fermentation cauldron
CN106110932A (en) A kind of intelligent and high-efficiency chemical industry dissolver
CN206103737U (en) Vacuum homogenizing emulsifying machine
CN105647787B (en) A kind of biological surfactant microemulsion production system used for cosmetic
CN208372948U (en) A kind of auger tank
CN206791573U (en) Equipment for bee product processing
CN208636652U (en) A kind of preparation facilities of organic photoresist stripper
CN209618973U (en) Supercritical water oxidation treatment system
CN205109468U (en) Fruity water beverage preparation is with allotment jar
CN105664819A (en) Microemulsion reactor for biological surfactant microemulsion production
EP1609779A1 (en) Process for producing carotenoid emulsion
CN108905932B (en) Experimental device suitable for gas-liquid interface reaction and using method thereof
CN207958380U (en) A kind of cell technique vaccine manufacture system
CN204602017U (en) A kind of eye drops dosing vacuum homogeneous emulsifying machine group
CN220370604U (en) Taurine decoloration filtration system
CN216824922U (en) Adsorption device
CN221359588U (en) Stirring device for preventing deposition of essence milk material
CN209108972U (en) A kind of FAU zeolite membrane circulation preparation facilities for CO2 capture
CN209501449U (en) A kind of vacuum emulsification device
CN209178181U (en) A kind of organic high-salinity wastewater processing
CN207451999U (en) A kind of combined type reaction system for preparing aqueous Stripable paint
JPS6058233A (en) Apparatus for holding and mixing pasturized suspension and solution

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right

Effective date of registration: 20180906

Address after: 350299 S03 1 storefront, 99 of Chaoyang North Road, Changle District, Fuzhou, Fujian.

Applicant after: Fuzhou Changle Stock Technology Co., Ltd.

Address before: 246620 Sanhe street, 055 Town, Yuexi County, Anqing, Anhui

Applicant before: Cheng Yehong

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20191121

Address after: 064400 Workshop No. 29, Fuda Small and Medium-sized Enterprise Park, Qian'an High-tech Industrial Development Zone, Tangshan City, Hebei Province

Patentee after: Zhongke Kangyuan (Tangshan) Biotechnology Co., Ltd.

Address before: 350299 S03 1 storefront, 99 of Chaoyang North Road, Changle District, Fuzhou, Fujian.

Patentee before: Fuzhou Changle Stock Technology Co., Ltd.

TR01 Transfer of patent right