CN102732417A - Emulsifying-type aerobic fermentation tank - Google Patents

Emulsifying-type aerobic fermentation tank Download PDF

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CN102732417A
CN102732417A CN2012102020585A CN201210202058A CN102732417A CN 102732417 A CN102732417 A CN 102732417A CN 2012102020585 A CN2012102020585 A CN 2012102020585A CN 201210202058 A CN201210202058 A CN 201210202058A CN 102732417 A CN102732417 A CN 102732417A
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pipe
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CN102732417B (en
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卢行娥
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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
    • 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
    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06—Nozzles; Sprayers; Spargers; Diffusers

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Abstract

The present invention discloses an emulsifying-type aerobic fermentation tank. According to the aerobic fermentation tank in the prior art, increase of compressed air consumption and improvement of stirring motor power can not significantly increase specific yield, and can cause energy consumption increasing, product cost improving, equipment cost increasing and operating environment deterioration. The emulsifying-type aerobic fermentation tank of the present invention comprises a tank body and a gas-liquid mixing circulation apparatus, wherein the gas-liquid mixing circulation apparatus is located inside the tank body, and has at least two stages of gas-liquid mixers. The gas-liquid mixing circulation apparatus is arranged vertically. The tank body is provided with a tank body gas inlet pipe and a fermented liquid inlet pipe. The tank is characterized in that: a self-suction air ejection emulsifying supercharging device is arranged between the gas-liquid mixing circulation apparatus and the inner wall of the tank body. With the tank of the present invention, oxygen utilization rate, mass transfer rate, dissolved oxygen coefficient and specific yield are improved, energy is substantially saved, the equipment is simplified, the microbiological contamination rate is reduced, the equipment cost and the maintenance cost are reduced, and the service life of the fermentation tank is prolonged.

Description

The emulsifying-type aerobic fermentation tank
Technical field
The present invention relates to biotechnology aerobic fermentation field, specifically a kind of emulsifying-type aerobic fermentation tank.
Background technology
Fermentor tank is a crucial biochemical reaction equipment in the aerobic fermentation industrial production, and in biological fermentation was produced, the transmission whipping appts that has the multi-stage mechanical whisking appliance in generally adopting now jar and jar end were provided with the general form fermentor tank of various ways breather.In biological fermentation process, aerobic bacterial classification needs that airborne oxygen grows, metabolism and output meta-bolites, to this, fully dissolved oxygen this be to produce bacterium vitality and the necessary condition of synthetic product.In production practice; In order to satisfy the dissolved oxygen content of aerobic mikrobe, making it to obtain required meta-bolites increases unit output, and adopting usually increases pressurized air consumption and the method that increases agitator motor power (improve mixing speed, increase whisking appliance quantity and increase stirrer diameter); In the hope of obtaining in the fermented liquid more polyoxy amount; Reduce bubble diameter, increase number of bubbles, contact specific surface area between increase gas, liquid, improve dissolved oxygen coefficient and unit output.Yet any type of breather of general form fermentor tank, its bubble diameter increases along with the increase of air flow, and the foam rate increase, improves the pulverizing that mixing speed helps bubble, but after bubble diameter arrives the some amount level, improves irrelevant with mixing speed.Because the mass transport mechanism of general form fermentor tank is the bubbling mass transfer, its flow characteristics is a plug flow, and it certainly exists the drawback that coefficient of oxygen utilization is low, dissolved oxygen coefficient is low.Therefore increase the pressurized air consumption and increase agitator motor power to raising unit output and not obvious, and cause energy consumption to increase, product cost improves, and equipment manufacturing cost increases and the operating environment deterioration.
Summary of the invention
Technical problem to be solved by this invention is to overcome the defective that above-mentioned prior art exists; Provide a kind of and not only do not had the gearing whipping appts, but also can reduce the emulsifying-type aerobic fermentation tank of pressurized air consumption; It has can make full use of the gas-liquid injection emulsifier unit that the energy that gets into the fermentor tank compressed air is realized the emulsification mass transfer; Utilize and feed jar energy air self-suction of interior fermented liquid and realize that the air self-suction of emulsification mass transfer, supercharging sprays the emulsification supercharging device; The gas-liquid mixed circulating device that the severe that makes full use of gas-liquid mixture is poor, static pressure difference and current difference are realized the changeable repeatedly recycle to extinction campaign of full bed small bubbles crowd emulsus stream; Improve coefficient of oxygen utilization, mass transfer velocity, dissolved oxygen coefficient and unit output, cut down the consumption of energy, reduce product cost significantly and improve production management and operating environment.
For this reason; The present invention adopts following technical scheme: the emulsifying-type aerobic fermentation tank; Comprise tank body and be positioned at jar intravital gas-liquid mixed circulating device of secondary gas liquid mixer at least that has, gas-liquid mixed circulating device vertically is provided with, and has tank body inlet pipe and fermented liquid inlet pipe on the tank body; It is characterized in that: be provided with an air self-suction between the inwall of said gas-liquid mixed circulating device and tank body and spray the emulsification supercharging device
This air self-suction sprays the emulsification supercharging device and comprises a plurality of tail pipes, a plurality of air intake pipe, a plurality of arm, an endless tube, a liquid-inlet pipe and at least two liquid gas emulsification supercharging blowers; Tail pipe, air intake pipe and arm are consistent with the number of liquid gas emulsification supercharging blower; Liquid gas emulsification supercharging blower vertically is provided with; Described liquid gas emulsification supercharging blower comprises nozzle, inlet pipe, mixing section and is positioned at the diffuser tube of mixing section below; Nozzle is connected on the mixing section and the outlet of nozzle is positioned at mixing section, and inlet pipe is connected with mixing section outer wall tangential and the two communicates;
Be connected with endless tube on described arm upper end and the liquid-inlet pipe and communicate; The liquid-inlet pipe lower end is connected with the fermented liquid inlet pipe and communicates; The arm lower end is connected with the nozzle of liquid gas emulsification supercharging blower and communicates; Air intake pipe is connected with the inlet pipe of liquid gas emulsification supercharging blower and communicates, and the inlet of tail pipe is connected with the outlet of liquid gas emulsification supercharging blower diffuser tube and communicates, and the outlet of tail pipe is connected with the second stage gas liquid mixer tangent line of gas-liquid mixed circulating device and communicates.
As the further of technique scheme improved and replenish, the present invention takes following technical measures:
Described air intake pipe is positioned at tank body (utilize jar an intravital air carry out self-priming) or outer end and stretches out in tank body outer (can external blower fan, the pressurized air after the sterilization is sent in the air intake pipe, carry out self-priming).
Described gas-liquid mixed circulating device is made up of first step gas liquid mixer, second stage gas liquid mixer, third stage gas liquid mixer and web plate, adopts web plate affixed between the adjacent two-stage gas liquid mixer.
Described first step gas liquid mixer is formed by connecting collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is 0.2～0.5 times of throat pipe diameter; Second stage gas liquid mixer is formed by connecting collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is 0.5～1.0 times of throat pipe diameter; Third stage gas liquid mixer is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the angle of throat of its collapsible tube is 45～90 °, the flare angle of convergent divergent channel is 20～60 °, length of throat is 2～10 times of throat pipe diameter.
In the described liquid gas emulsification supercharging blower, the angle of throat of nozzle is 10～20 °, diffuser tube is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the angle of throat of collapsible tube is 15～45 °, convergent divergent channel flare angle be 5～15 °, length of throat is 10～40 times of throat pipe diameter, the trunnion of diffuser tube is 3～15:1 with the cross-sectional area of nozzle throat ratio.
The bottom of said tank body be provided with one be positioned at gas-liquid mixed circulating device below the gas-liquid injection emulsifier unit; This gas-liquid injection emulsifier unit is made up of a plurality of bend pipes, a plurality of flange, an endless tube, an inlet pipe and two circle gas-liquid emulsor groups at least; Bend pipe is connected with endless tube with inlet pipe and communicates; Inlet pipe is connected with the tank body inlet pipe and communicates, and every circle gas-liquid emulsor group is furnished with two gas-liquid emulsors at least, and the number of bend pipe and flange is consistent with the number of gas-liquid emulsor; All on the tangent to periphery of same xsect, every gas-liquid emulsor is connected fixing the Way out of all gas-liquid emulsors with flange.
Described gas-liquid emulsor is made up of nozzle, flange, web plate and diffuser tube; Nozzle is fixed on the flange; Flange and diffuser tube are fixing with the web plate welding; Diffuser tube is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the outlet of nozzle is positioned at collapsible tube, and the angle of throat of collapsible tube is 30～90 °, the flare angle of convergent divergent channel is 7～15 °, length of throat is 6～15 times of throat pipe diameter, the angle of throat of nozzle is 10 °～20 °, diffuser tube is 8～15:1 with the cross-sectional area ratio of nozzle throat, the angle of gas-liquid emulsor and horizontal plane is 0～20 °, 0～15 °Or-10～0 °
In the gas-liquid injection emulsifier unit, a plurality of gas-liquid emulsors of every circle gas-liquid emulsor group are along the circumference uniform distribution.
Above gas-liquid mixed circulating device, be provided with at least one steady liquid froth breaking sieve plate.
Spray in the emulsification supercharging device at air self-suction, a plurality of tail pipes outlets of liquid gas emulsification supercharging blower are all on the tangent to periphery direction that is positioned at same xsect of second stage gas liquid mixer, and a plurality of tail pipe exports along the circumference uniform distribution.
Emulsifying-type aerobic fermentation tank of the present invention; Adopt gas-liquid injection emulsifier unit, air self-suction injection emulsification supercharging device and gas-liquid mixed circulating device to replace having the gearing whipping appts of multi-stage mechanical whisking appliance, and reduce pressurized air consumption, particularly air self-suction and spray the emulsification supercharging device; Make full use of the transmitting and converting that the energy that feeds fermentor tank compressed air and fermented liquid carries out quality and energy; Traditional bubbling mass transport mechanism is changed into the emulsification mass transport mechanism, the oxygen in the tank deck emission gases is sucked utilization once more, the flow characteristics of gas-liquid mixture is changed repeatedly into the emulsification stream of changeable recycle to extinction campaign from plug flow; Coefficient of oxygen utilization, mass transfer velocity, dissolved oxygen coefficient and unit output have not only been improved; And practiced thrift the energy significantly, and simplified equipment, reduce the microbiological contamination rate, reduced equipment manufacturing cost and maintenance cost, prolonged fermentor tank work-ing life; Eliminate the vibrations of tank body when noise and steam are directly real to disappear simultaneously, improved production management and operating environment.
Below in conjunction with Figure of description and embodiment the present invention is further described.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the structural representation of gas-liquid injection emulsifier unit of the present invention.
Fig. 3 is that the A of Fig. 2 is to view.
Fig. 4 is the structural representation of gas-liquid emulsor of the present invention.
Fig. 5 is a gas-liquid mixed circulating device structural principle synoptic diagram of the present invention.
Fig. 6 sprays the structural representation of emulsification supercharging device for air self-suction of the present invention.
Fig. 7 is that the B of Fig. 6 is to view.
Fig. 8 is the structural representation of liquid gas emulsification supercharging blower of the present invention.
Embodiment
Emulsifying-type aerobic fermentation tank as shown in Figure 1; Tank body 6 is the vertical enclosed containers of long tubular, tank body 6 and skirt 1 affixed being integral, and the top of tank body 6 has interfaces such as opening for feed 14, visor 15, strain nutrition import 16, venting port 17, manhole 18; The bottom of tank body 6 has overhanging jar of outer fermented liquid outlet pipe 21; The affixed special-shaped pipe racks of tank body 6 outer walls (or chuck) interchanger 8, tank body 6 have tank body inlet pipe 4 and fermented liquid inlet pipe 19, and inner coil pipe interchanger 7 is set in the tank body 6.
Shown in Fig. 2-3; Has gas-liquid injection emulsifier unit 2 in tank body 6 bottoms; This gas-liquid injection emulsifier unit 2 is made up of a plurality of bend pipe 22, a plurality of flange 23, an endless tube 25, an inlet pipe 26 and three circle gas-liquid emulsor groups 29,30,31; Bend pipe 22 is connected with endless tube 25 with inlet pipe 26 and communicates, and inlet pipe 26 is connected with tank body inlet pipe 4 and communicates, and the assembly of every circle gas-liquid emulsor has 8 gas-liquid emulsors; All on the tangent to periphery of same xsect, every gas-liquid emulsor is connected fixing its Way out with flange 23.Endless tube 25 is connected fixing with tank body 6 bottoms through web member 20.Upper, middle and lower three circle gas-liquid emulsor groups 29,30,31 are housed on endless tube 25, and every circle gas-liquid emulsor group 29,30,31 corresponding gas- liquid emulsors 24,27,28 are connected fixing with flange 23 usefulness bolts.Many gas- liquid emulsors 24,27,28 in every circle gas-liquid emulsor group 29,30,31 are along the circumference uniform distribution, and all on the tangent to periphery of same xsect, gas-liquid emulsor 24 is 0～20 with the angle of horizontal plane to its Way out °, the angle 0～15 of gas-liquid emulsor 27 and horizontal plane °, gas-liquid emulsor 28 is-10～0 with the angle of horizontal plane °
As shown in Figure 4, the gas-liquid emulsor is made up of nozzle 32, flange 33, web plate 34 and diffuser tube 35.Nozzle 32 is fixed on the flange 33, and nozzle 32 separates with diffuser tube 35, by web plate 34 flange 33 is connected fixingly with diffuser tube 35, and flange 33 is connected with flange 23 usefulness bolts in the gas-liquid injection emulsifier unit to be fixed.Diffuser tube 35 has collapsible tube, trunnion and convergent divergent channel, and the angle of throat of collapsible tube is 30～90 °, convergent divergent channel flare angle be 7～15 °, length of throat is (6～15) times throat pipe diameter; The angle of throat of nozzle 32 is 10～20 °, trunnion is (8～15) with the cross-sectional area ratio of nozzle throat: 1.
As shown in Figure 5; Above gas-liquid injection emulsifier unit 2, has gas-liquid mixed circulating device 3; This gas-liquid mixed circulating device 3 is made up of first, second and third grade gas liquid mixer 36,38,40; First, second and third grade gas liquid mixer 36,38,40 threes separate; Connect fixing first and second grade gas liquid mixer 36,38 by web plate 37, web plate 39 connects fixing second and third grade gas liquid mixer 38,40, and web plate 37,39 is with first, second and third grade gas liquid mixer 36,38,40 affixed being integral; The first step gas liquid mixer 36 that is positioned at foot is fixing with following web member 5 welding of tank body 6 usefulness; The third stage gas liquid mixer 40 that is positioned at topmost is fixing with 9 welding of tank body 6 usefulness upper connectors, and the second stage gas liquid mixer 38 that is positioned at the middle part is fixing with following web member 5 usefulness shaped steel welding, above gas-liquid mixed circulating device 3, has at least one steady liquid froth breaking sieve plate 12.First step gas liquid mixer 36 is made up of collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is (0.2～0.5) times throat pipe diameter; Second stage gas liquid mixer 38 is made up of collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is (0.5～1.0) times throat pipe diameter; Third stage gas liquid mixer 40 is made up of collapsible tube, trunnion and convergent divergent channel, and the angle of throat of its collapsible tube is 45～90 °, the flare angle of convergent divergent channel is 20～60 °, length of throat is (2～10) times throat pipe diameter, gas-liquid mixed circulating device is vertically installed.
As shown in Figure 1, have vertically arranged air self-suction in the space between gas-liquid mixed circulating device 3 and inner coil pipe interchanger 7 and spray emulsification supercharging device 11.Shown in Fig. 6-7; Air self-suction sprays emulsification supercharging device 11 by tail pipe 41, liquid gas emulsification supercharging blower 42,47,48, air intake pipe 43; Arm 44; Endless tube 45 constitutes with liquid-inlet pipe 46, and endless tube 45 and fermented liquid inlet pipe 19 affixed communicating, endless tube 45 are connected fixing with tank body 6 usefulness web members 10; Air intake pipe 43 and tank body 6 usefulness web plates 13 are affixed and be connected with liquid gas emulsification supercharging blower 42,47,48 and communicate, tail pipe 41 be connected with liquid gas emulsification supercharging blower 42,47,48 communicate and with gas-liquid mixed circulating device 3 in second stage gas liquid mixer 38 the trunnion tangent line is affixed communicates.The zig-zag suction port of air intake pipe 43 is higher than visor 15.
As shown in Figure 8, liquid gas emulsification supercharging blower is made up of nozzle 49, inlet pipe 50, mixing section 51 and diffuser tube 52.Nozzle 49 is fixed in mixing section 51, and inlet pipe 50 tangent lines are fixed in mixing section 51 and the two communicates, and liquid gas emulsification supercharging blower adopts bolt to be connected fixing with tail pipe 41, air intake pipe 43 and arm 44 respectively and is interconnected.The angle of throat of nozzle 49 is 10～20 °, diffuser tube 52 has collapsible tube, trunnion and convergent divergent channel, and the angle of throat of its collapsible tube is 15～45 °, convergent divergent channel flare angle be 5～15 °, length of throat is (10～40) times throat pipe diameter, the xsect of diffuser tube 52 trunnions and nozzle 49 throats is than being (3～15): 1.
When emulsifying-type aerobic fermentation tank of the present invention uses; By feed pump substratum feed liquid in the dosing chamber is sent in the jar through opening for feed 14; After sterilization, ventilation cooling (steam, air must get into gas-liquid injection emulsifier unit 2), bacterial classification is cultivated in strain nutrition mouth 16 immigration jars.0.07 the aseptic compressed air of～0.35Mpa pressure is sent into through tank body inlet pipe 4 and is respectively welded bend pipe 22 on gas-liquid injection emulsifier unit 2 endless tubes 25, and gets into respectively and respectively enclose the gas- liquid emulsor 24,27,28 of gas-liquid emulsor group 29,30,31.When air quantity is V p, pressure is P pPressurized air from gas-liquid emulsor nozzle 32 (W at a high speed 1) ejection, when the pressurized air static energy is transformed into the speed ability, be γ with severe 1, pressure is P 1Fermented liquid V LSuck and together get into the diffuser tube 35 of gas-liquid emulsor, in the collapsible tube of diffuser tube 35, trunnion, gas, liquid two-phase are expanded to fierce mixing concussion and are produced pressure foamization and aerodynamic force foamization by preliminary mixing, and its foam result makes the entering air V pWith the fermented liquid V that is inhaled into LImpact is dispersed into a large amount of small grain crowds, causes the great and surperficial emulsification mass transfer interface of bringing in constant renewal between gas, liquid, and airborne oxygen is fully used; Mass transfer velocity, dissolved oxygen coefficient improve; In the convergent divergent channel of diffuser tube 35, along with the increase of expansion section, gas-liquid mixture flow velocity (W 2) decline, static energy is able to progressively recover, by means of the poor (P of static pressure of gas-liquid emulsor diffuser tube entry and exit places gas-liquid mixture 1>P 2) and the poor (γ of severe 1>γ 2); The radially loopful stream motion that the gas-liquid mixed deposits yields is gone round and begun again; Seeing that gas- liquid emulsor 24,27,28 diffuser tubes 35 outlets of every circle gas-liquid emulsor group 29,30,31 are all on the tangent to periphery direction of same xsect; Make gas-liquid mixed stream spirrillum swirling motion, increased the movement locus of micro-bubble in fermented liquid, increased the duration of contact of oxygen and mycelia.Screwing out pressure from 2 sprays of gas-liquid injection emulsifier unit is P 2, severe is γ 2Gas-liquid mixture (V p+ V L) all get into gas-liquid mixed circulating device 3 bottom first step gas liquid mixer 36 collapsible tubes, under the spray effect of revolving of gas-liquid mixed stream, by means of the poor (P of static pressure of place, gas liquid mixer at different levels 36,38,40 entry and exit gas-liquid mixture 3>P 4>P 5>P 6), the poor (γ of severe 3>γ 4>γ 5>γ 6), velocity contrast (W 3>W 4>W 5) and air self-suction sprays, and tail pipe 41 tangent lines get into speed ability and the pressure ability that second stage gas liquid mixer 38 gas-liquid mixed flow, three grades of injection gas-liquid mixtures (fermented liquid) V in the emulsification supercharging device 11 3, V 4, V 5, realizing that gas-liquid mixture axially mixes, the swirling motion of internal recycle, increase gas, liquid two alternate mixture strengties contact opportunity with oxygen with mycelia, make the oxygen in the gas phase obtain recycled for multiple times.The aggravation of stirring along with the cellular spherical micro-bubble crowd's of full bed rising, coalescence and gas-liquid emulsus stream; Gas, liquid mixture are behind steady liquid froth breaking sieve plate 12; Bubble is overflowed from cultivating liquid level, and forms the gas-phase space of 0.015～0.05Mpa pressure emission gases at tank body 6 tops.Because airborne oxygen is the gas that is insoluble in water; Solubleness is not high in fermented liquid; Its utilization ratio is very low; Therefore in the gas-phase space of emission gases, still contain a large amount of oxygen parts, in order to utilize the oxygen in the emission gases again, to improve mass transfer velocity, dissolved oxygen coefficient and unit output; By the fermentation liquid pump through fermented liquid outlet pipe 21 tank body 6 inner bottom part fermented liquids are sucked and send into tank body 6 bottom fermented liquid inlet pipes 19, air self-suction sprays each branch pipe welded directly to the run pipe 44 on liquid-inlet pipe 46, endless tube 45 and the endless tube 45 in the emulsification supercharging device 11, sends into liquid gas emulsification supercharging blower 42,47,48 more respectively.When flow is V L, pressure is P L(0.35～0.6Mpa) fermented liquid is from liquid gas emulsification supercharging blower nozzle 49 high speed (W 6) ejection, when the static energy of fermented liquid changes the speed ability into, be P with pressure in the tank body 6 top gas-phase spaces p(0.015～0.05Mpa) and contain the emission gases V of a large amount of oxygen pSuck voluntarily, through air intake pipe 43, tangent line gets into the mixing section 51 of liquid gas emulsification supercharging blower, under the continuous injection effect of fermented liquid, with the emission gases V that sucks pThe diffuser tube 52 of bringing liquid gas emulsification supercharging blower into carries out liquid, gas two alternate quality and transmission ofenergy conversion; Supervene the intensive friction, vibrate, break and foamization; Make fermented liquid and suck gas and become a large amount of small grain crowds, form the contact interface that height turbulence between liquid, gas and surface are brought in constant renewal in, increase the gas-to-liquid contact specific surface area by impact grinding once more; Realize the emulsification mass transfer; Along with the growth of diffuser tube 52 length of throat and dwindling of convergent divergent channel flare angle, gas-liquid mixed concussion and emulsification are prolonged duration of contact, and make liquid gas emulsification outlet pressure of the booster P L.PIncrease (P L.P>P P), fermented liquid and the enterprising flow characteristics that goes out down of suction gas all help improving the transmission of oxygen in fermented liquid in addition.Thereafter along with the increase gradually of expanding section, the flow velocity W of gas-liquid mixture 7Progressively descend; Static energy is able to progressively recover; Have certain speed can with pressure can flow through second stage gas liquid mixer 38 trunnions of tail pipe 41 tangent lines entering gas-liquid mixed circulating device 3 of gas-liquid emulsus carry out cyclic motion repeatedly; Final bubble is overflowed and is cultivated liquid level, discharges from venting port 17 through gas-phase space.Fermented liquid, is pumped to extraction workshop section through fermented liquid outlet pipe 21 usefulness fermented liquids and obtains through refining product after reaching the desired productive capacity of zymotechnique through the cultivation of certain hour.
The above only is preferred embodiment of the present invention, is not structure of the present invention is done any pro forma restriction.Every foundation technical spirit of the present invention all falls in protection scope of the present invention any simple modification, equivalent variations and modification that above embodiment did.

Claims (10)

1. emulsifying-type aerobic fermentation tank; Comprise tank body (6) and be positioned at the gas-liquid mixed circulating device of secondary gas liquid mixer (3) at least that has of tank body (6); Gas-liquid mixed circulating device (3) is vertical to be provided with; Have tank body inlet pipe (4) and fermented liquid inlet pipe (19) on the tank body (6), it is characterized in that: be provided with an air self-suction between the inwall of said gas-liquid mixed circulating device (3) and tank body (6) and spray emulsification supercharging device (11)
This air self-suction sprays emulsification supercharging device (11) and comprises a plurality of tail pipes (41), a plurality of air intake pipe (43), a plurality of arm (44), an endless tube (45), a liquid-inlet pipe (46) and at least two liquid gas emulsification supercharging blowers; Tail pipe (41), air intake pipe (43) and arm (44) are consistent with the number of liquid gas emulsification supercharging blower; Liquid gas emulsification supercharging blower vertically is provided with; Described liquid gas emulsification supercharging blower comprises nozzle (49), inlet pipe (50), mixing section (51) and is positioned at the diffuser tube (52) of mixing section (51) below; Nozzle (49) is connected on the mixing section (51) and the outlet of nozzle (49) is positioned at mixing section (51), and inlet pipe (50) is connected with mixing section (51) outer wall tangential and the two communicates;
Be connected with endless tube (45) on described arm (44) upper end and the liquid-inlet pipe (46) and communicate; Liquid-inlet pipe (46) lower end is connected with fermented liquid inlet pipe (19) and communicates; Arm (44) lower end is connected with the nozzle (49) of liquid gas emulsification supercharging blower and communicates; Air intake pipe (43) is connected with the inlet pipe (50) of liquid gas emulsification supercharging blower and communicates; The inlet of tail pipe (41) is connected with the outlet of liquid gas emulsification supercharging blower diffuser tube (52) and communicates, and the outlet of tail pipe (41) is connected with second stage gas liquid mixer (38) tangent line of gas-liquid mixed circulating device (3) and communicates.
2. emulsifying-type aerobic fermentation tank according to claim 1 is characterized in that, described air intake pipe (43) is positioned at tank body (6) or the outer end stretches out in outside the tank body (6).
3. emulsifying-type aerobic fermentation tank according to claim 1 and 2; It is characterized in that; Described gas-liquid mixed circulating device (3) is made up of first step gas liquid mixer (36), second stage gas liquid mixer (38), third stage gas liquid mixer (40) and web plate, adopts web plate affixed between the adjacent two-stage gas liquid mixer.
4. emulsifying-type aerobic fermentation tank according to claim 3 is characterized in that, described first step gas liquid mixer (36) is formed by connecting collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is 0.2～0.5 times of throat pipe diameter; Second stage gas liquid mixer (38) is formed by connecting collapsible tube and trunnion, and its angle of throat is 45～90 °, length of throat is 0.5～1.0 times of throat pipe diameter; Third stage gas liquid mixer (40) is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the angle of throat of its collapsible tube is 45～90 °, the flare angle of convergent divergent channel is 20～60 °, length of throat is 2～10 times of throat pipe diameter.
5. emulsifying-type aerobic fermentation tank according to claim 1 and 2 is characterized in that, in the described liquid gas emulsification supercharging blower, the angle of throat of nozzle (49) is 10～20 °, diffuser tube (52) is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the angle of throat of collapsible tube is 15～45 °, convergent divergent channel flare angle be 5～15 °, length of throat is 10～40 times of throat pipe diameter, the cross-sectional area ratio of the trunnion of diffuser tube (52) and nozzle (49) throat is 3～15:1.
6. emulsifying-type aerobic fermentation tank according to claim 1 and 2 is characterized in that, the bottom of said tank body (6) be provided with one be positioned at gas-liquid mixed circulating device (3) below gas-liquid injection emulsifier unit (2),
This gas-liquid injection emulsifier unit (2) is made up of a plurality of bend pipes (22), a plurality of flange (23), an endless tube (25), an inlet pipe (26) and two circle gas-liquid emulsor groups at least; Bend pipe (22) is connected with endless tube (25) with inlet pipe (26) and communicates; Inlet pipe (26) is connected with tank body inlet pipe (4) and communicates; Every circle gas-liquid emulsor group is furnished with two gas-liquid emulsors at least; The number of bend pipe and flange is consistent with the number of gas-liquid emulsor, and all on the tangent to periphery of same xsect, every gas-liquid emulsor is connected fixing the Way out of all gas-liquid emulsors with flange (23).
7. emulsifying-type aerobic fermentation tank according to claim 6; It is characterized in that described gas-liquid emulsor is made up of nozzle (32), flange (33), web plate (34) and diffuser tube (35), nozzle (32) is fixed on the flange (33); Flange (33) and diffuser tube (35) are fixing with web plate (34) welding; Diffuser tube (35) is connected in sequence by collapsible tube, trunnion and convergent divergent channel, and the outlet of nozzle (32) is positioned at collapsible tube, and the angle of throat of collapsible tube is 30～90 °, the flare angle of convergent divergent channel is 7～15 °, length of throat is 6～15 times of throat pipe diameter, the angle of throat of nozzle (32) is 10 °～20 °, diffuser tube (35) is 8～15:1 with the cross-sectional area ratio of nozzle (32) throat, the angle of gas-liquid emulsor and horizontal plane is 0～20 °, 0～15 °Or-10～0 °
8. emulsifying-type aerobic fermentation tank according to claim 6 is characterized in that, in the gas-liquid injection emulsifier unit (2), a plurality of gas-liquid emulsors of every circle gas-liquid emulsor group are along the circumference uniform distribution.
9. emulsifying-type aerobic fermentation tank according to claim 1 and 2 is characterized in that, is provided with at least one steady liquid froth breaking sieve plate (12) in gas-liquid mixed circulating device (3) top.
10. emulsifying-type aerobic fermentation tank according to claim 1 and 2; It is characterized in that; Spray in the emulsification supercharging device (11) at air self-suction; The outlet of a plurality of tail pipes (41) of liquid gas emulsification supercharging blower is all on the tangent to periphery direction that is positioned at same xsect of second stage gas liquid mixer (38), and a plurality of tail pipe (41) outlet is along the circumference uniform distribution.
CN 201210202058 2012-06-15 2012-06-15 Emulsifying-type aerobic fermentation tank Expired - Fee Related CN102732417B (en)

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CN105505749A (en) * 2016-03-04 2016-04-20 江南大学 Air-liquid dual injection type airlift loop reactor
CN106190786A (en) * 2016-08-31 2016-12-07 吕建军 A kind of multiple spot air sparger and apply its fermentation tank
CN106190787A (en) * 2016-08-31 2016-12-07 吕建军 The spiral air distributor of a kind of fermentation tank and fermentation tank
CN106190795A (en) * 2016-09-19 2016-12-07 浙江诚信医化设备有限公司 A kind of fermentation tank of band air sparger
CN106381267A (en) * 2016-08-31 2017-02-08 西安若翰生物饲料有限公司 Simple efficient solid fermentation device
CN112410222A (en) * 2020-11-03 2021-02-26 江南大学 Multi-chamber bubble tower bioreactor for animal cell culture
CN113207964A (en) * 2021-05-28 2021-08-06 童军 Dairy product fermentation process
CN115181659A (en) * 2022-09-14 2022-10-14 山东鹤来生物科技有限公司 Probiotic fermentation tank
CN116925897A (en) * 2023-09-15 2023-10-24 龙牌食品股份有限公司 Aeration-cooling device for making yeast by disc

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CN202107697U (en) * 2011-05-23 2012-01-11 陆飞浩 Swirling flow airlift fermentation tank
CN202164295U (en) * 2011-07-22 2012-03-14 山东鲁抗舍里乐药业有限公司 Circular spray-type aerobic fermentation device
CN202595129U (en) * 2012-06-15 2012-12-12 卢行娥 Emulsification type aerobic fermentation tank

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CN2890062Y (en) * 2005-08-23 2007-04-18 南京工业大学 Cyclone and inflation combined biochemical reactor
CN202107697U (en) * 2011-05-23 2012-01-11 陆飞浩 Swirling flow airlift fermentation tank
CN202164295U (en) * 2011-07-22 2012-03-14 山东鲁抗舍里乐药业有限公司 Circular spray-type aerobic fermentation device
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105505749A (en) * 2016-03-04 2016-04-20 江南大学 Air-liquid dual injection type airlift loop reactor
CN106190786A (en) * 2016-08-31 2016-12-07 吕建军 A kind of multiple spot air sparger and apply its fermentation tank
CN106190787A (en) * 2016-08-31 2016-12-07 吕建军 The spiral air distributor of a kind of fermentation tank and fermentation tank
CN106381267A (en) * 2016-08-31 2017-02-08 西安若翰生物饲料有限公司 Simple efficient solid fermentation device
CN106190795A (en) * 2016-09-19 2016-12-07 浙江诚信医化设备有限公司 A kind of fermentation tank of band air sparger
CN112410222A (en) * 2020-11-03 2021-02-26 江南大学 Multi-chamber bubble tower bioreactor for animal cell culture
CN112410222B (en) * 2020-11-03 2022-02-01 江南大学 Multi-chamber bubble tower bioreactor for animal cell culture
CN113207964A (en) * 2021-05-28 2021-08-06 童军 Dairy product fermentation process
CN115181659A (en) * 2022-09-14 2022-10-14 山东鹤来生物科技有限公司 Probiotic fermentation tank
CN116925897A (en) * 2023-09-15 2023-10-24 龙牌食品股份有限公司 Aeration-cooling device for making yeast by disc
CN116925897B (en) * 2023-09-15 2023-12-05 龙牌食品股份有限公司 Aeration-cooling device for making yeast by disc

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