CN202107697U

CN202107697U - Swirling flow airlift fermentation tank

Info

Publication number: CN202107697U
Application number: CN 201120178275
Authority: CN
Inventors: 陆飞浩
Original assignee: Individual
Current assignee: Individual
Priority date: 2011-05-23
Filing date: 2011-05-23
Publication date: 2012-01-11
Anticipated expiration: 2021-05-23

Abstract

The utility model discloses a swirling flow airlift fermentation tank, which comprises a tank body, an air inlet device, an air exhaust device and a cooling device. An air inlet pipe and an air exhaust pipe are arranged on the tank body. The air inlet pipe is connected with the air inlet device. The air exhaust pipe is connected with the air exhaust device. The fermentation tank is characterized in that the air inlet pipe is arranged at the intermediate position of the bottom of the tank body or close to the bottom of the tank body. The air exhaust pipe is arranged at the intermediate position of the top of the tank body. The air inlet device is a swirling flow mixer arranged at the bottom of the interior of the tank body or close to the bottom of the tank body and is connected with the air inlet pipe. A diversion device is arranged above the swirling flow mixer. The diversion device adopts a cylindrical structure and the two ends of the diversion device are equipped with openings. The diversion device is longitudinally arranged on the axis of the tank body. The swirling flow airlift fermentation tank adopts no stirring device and is concise in structure and relatively low in ventilation pressure. Meanwhile, the fermentation tank enables gas and liquid to be in a swirling state and well mixed. The fermentation tank also has the advantages of good gas-liquid mixing effect, low energy consumption and high efficiency in gas exhaust, cleaning and fermentation and is suitable for the liquid submerged fermentation of aerobic microorganisms.

Description

A kind of eddy flow airlift fermentor

Technical field

The utility model relates to a kind of fermentor tank, and especially a kind of being applied in the industrialized production is as the eddy flow airlift fermentor of aerobic bacteria fermentation.

Background technology

Usually there are stirring system, cooling heat radiation system and ventilation gas barrier etc. in aerobic bacteria fermentor tank inside.Along with industry is produced the fermentation scale greatly and constantly enlarged, separate unit fermentor tank diameter, highly also be multiplied.The fermentor tank diameter increases to present 4m～10m from past 2m～4m; Height increases to present 10m～20m from past 5m～10m.Because square being directly proportional of power of agitator and stirrer diameter, so the fermentor tank volume enlarges afterwards that power of agitator rises at double, causes energy consumption significantly to increase.

For cutting down the consumption of energy; In recent years exploitation has multiple vertical no stirred fermentor, and it utilizes the compressed air pressure ability, makes the gas-liquid homogeneous and is converted into high-speed jet through fluidic device; Relend and help a jar interior guiding device, drive the fermented liquid circulation, fermentation process is evenly carried out in jar.But require air to advance the required pressure of air blow tank that pressure tank stirs greater than normal tape for transforming high-speed jet; Thus, though save power of agitator consumption, and the rising of air compressor machine top hole pressure causes power consumption to rise; This disappears, and that is long, and it is poor that the band effusive does not have the stirred fermentor energy-saving effect.Moreover part producing bacterium growth metabolism in the environment of high-speed jet is influenced, can not use this kind fermentor tank, so its practical ranges is very limited, needs to improve.

The utility model content

The utility model technical problem to be solved be to the above-mentioned state of the art and a kind of no whipping appts is provided, venting pressure is lower but can make gas-liquid be the eddy flow state, gas-liquid mixed is respond well, the eddy flow airlift fermentor of low-consumption high-efficiency.

The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of eddy flow airlift fermentor; It comprises inlet pipe, the vapor pipe that is provided with on tank body, diffuser, gas barrier, refrigerating unit and the said tank body, and said inlet pipe is connected with diffuser, and said vapor pipe is connected with gas barrier; It is characterized in that: said inlet pipe is located at the mid-way of tank base or near the tank base position; Said vapor pipe is located at the mid-way at tank body top, and said diffuser is a cyclone mixer, is located at jar intravital bottom perhaps near the tank base position; And be connected with inlet pipe; Above cyclone mixer, be provided with guiding device, said guiding device is the tubular structure of both ends open, is on the axis that vertically is arranged on tank body; Said jar of intravital fermentation gas-liquid is the eddy flow state and mixes under the effect of cyclone mixer, and makes inside and outside cyclic motion along guiding device.

As improvement, said guiding device is divided into several sections that arrange up and down in tank body, and the upper end of each section guiding device forms is convenient to the hole enlargement mouth that fermented liquid flows into.

As improvement; Said cyclone mixer comprises splendid attire fermented liquid and inner housing and the body skin of separating the gas-liquid import, and inner housing top or bottom communicate with inlet pipe, accordingly; The top of the top of body skin and bottom or body skin is provided with fluid inlet; The center of inner housing is circle-shaped some blades that are distributed with, and in inner housing, forms air-flow eddy flow passage, and forms the swirl channel of gas-liquid mixed between inner housing and the body skin.

As improvement, said refrigerating unit comprises first cooling jacket of being located at the tank body wall and second cooling jacket of being located at the guiding device wall.

Improve, said first cooling jacket is arranged on outer wall or the inwall or the inside and outside wall of tank body again, and said second cooling jacket is arranged on outer wall or the inwall or the inside and outside wall of guiding device.

Improve, said first cooling jacket and second cooling jacket adopt honeycomb fashion or flow channel type again, are to be connected by welding fabrication of thin-wall stainless steel laser.

Further improve; Said gas barrier comprises efficiently revolving and hits gas-liquid separator, liquid return tube and escape pipe; One end of said vapor pipe inserts fermentor tank top center, the other end and connects efficiently to revolve and hit gas-liquid separator, is connected with escape pipe and liquid return tube on the said gas-liquid separator, and the gas-liquid-solid mixture that is brought by vapor pipe is after separator is handled; The solid, liquid thing of separating passes back in the tank body through liquid return tube, and the gas of separating is discharged by escape pipe.

Further improve, the liquid outflow end of said liquid return tube is located at the central inlet place of jar intravital guiding device again, and is in below the initial liquid level of fermentation.

At last, said vapor pipe is provided with regulating valve.

Compared with prior art; The utility model adopts cyclone mixer as diffuser, replaces traditional ring pipe or ejector, makes air get into from the center; Water conservancy diversion through the vortex passage; Be eddy flow shape ejection, liquid is brought into wherein near attracting simultaneously, and is the emulsification shape after the gas Forced Mixing and derives; Simultaneously guiding device is set in tank body, makes the fermented liquid circulation more smooth and easy, dissolved oxygen increases; Not only at the tank body wall cooling jacket is set, at the guiding device wall cooling jacket is set also, make heat interchanging area big, flow rate of liquid is very fast relatively, good effect of heat exchange; Exhaust gas treatment device adopts efficiently to revolve and hits separator, and the solid-liquid thing of carrying secretly in the fermentation exhaust is separated backflow, makes exhaust gas cleaning, has both improved the fermentor tank utilization ratio, again environmental protection; And, help the generation and the extraction of tunning owing to there be not the infringement of mechanical shearing to microorganism cells; The eddy flow airlift fermentor of the utility model whipping appts simple for structure, no, venting pressure is lower but can make that gas-liquid is the eddy flow state, gas-liquid mixed is respond well and low-consumption high-efficiency; While exhaust gas cleaning, fermentation efficiency height; Synthesis energy saving can reach 20%～50%, is applicable to the aerobic bacteria liquid submerged fermentation.

Description of drawings

Fig. 1 is the structural representation of the eddy flow airlift fermentor of the utility model embodiment;

Fig. 2 a, 2b are the structural representation of the cyclone mixer of the utility model embodiment;

Fig. 3 a, 3b are the another kind of structural representation of the cyclone mixer of the utility model embodiment;

Fig. 4 a, 4b are the cooling jacket structural representation of the utility model embodiment, and wherein a is a flow channel type, and b is a honeycomb fashion.

Embodiment

Embodiment describes in further detail the utility model below in conjunction with accompanying drawing.

As shown in Figure 1; A kind of eddy flow airlift fermentor; Comprise vertical tank body cylindraceous 1, diffuser, gas barrier, guiding device and refrigerating unit, said tank body 1 is provided with the pipe joint of inlet pipe 11, vapor pipe 4 and various necessity, and said inlet pipe 11 is located at the central position of tank body 1 bottom or near the central position of tank body 1 bottom; Be connected with diffuser, the central position that said vapor pipe 4 is located at tank body 1 top is connected with gas barrier.

Shown in Fig. 2 a, 2b, said diffuser is a cyclone mixer 2, is located at bottom in the tank body 1, is adjacent to tank body 1 lower cover and installs and be connected with inlet pipe 11; The impeller of said cyclone mixer 2 similar centrifugal water pumps comprises splendid attire fermented liquid and the inner housing of separating the gas-liquid import 26 and body skin 25, and the top of said body skin 25 is provided with fluid inlet 21; Center in the said inner housing 26 is circle-shaped some blades 22 that are evenly distributed with; In inner housing 26, form air-flow eddy flow passage 23, and between body skin 25 and inner housing 26, form the swirl channel 24 of gas-liquid mixed, swirl channel 24 is extended with eddy flow passage 23 and is communicated with; Air gets into the eddy flow passage 23 of cyclone mixer 2 from inlet pipe 11; Simultaneously fermented liquid gets into from its fluid inlet 21, and gas-liquid two-phase is emulsion form after in vortex passage 24, being forced mixing, then to around rotary-jet; And upwards flow naturally; Speed is low than ejector therein owing to gas, and the pressure-losses is minimum, and the fermentor tank that therefore advances the stirring of ullage atmospheric pressure and common band is very nearly the same.

Shown in Fig. 3 a, 3b, be cyclone mixer 2 another mounting structures, cyclone mixer 2 unsettled being installed in above tank body 1 bottom; And near the bottom of tank body 1; Cyclone mixer 2 comprises splendid attire fermented liquid and the inner housing of separating the gas-liquid import 26 and body skin 25, and body skin 25 is provided with fluid inlet 21 near tank base center and top, and the top of inner housing 26 is connected with inlet pipe 11; The center of inner housing 26 is circle-shaped some blades 22 that are evenly distributed with; In inner housing 26, form air-flow eddy flow passage 23, and form the swirl channel 24 of gas-liquid mixed between inner housing 26 and the body skin 25, swirl channel 24 is converged with air-flow eddy flow passage 23 in inner housing 26 peripheries mutually.

As shown in Figure 1, above cyclone mixer 2, be provided with guiding device 3, said guiding device 3 is divided into two sections; Be respectively the thin-walled straight-tube shape structure of both ends open, vertically be arranged on the hub of tank body 1, the upper end of every section guiding device 3 forms is convenient to the hole enlargement mouth 31 that fermented liquid flows into; Because cyclone mixer 2 produces downward sucking action to liquid on it; In conjunction with guiding device 3, make the fermentation pot liquid produce the center downwards, circulating of making progress all around, this circulation is axial along fermentor tank; Also circumferential along fermentor tank; Macro manifestations is spiral escalation and decline, is different from the circulation of setting up through mechanical stirring in the common fermentation jar, also is different from the circulation that ejector drives through high-speed jet; The circulation that cyclone mixer causes does not cause microorganism cells to shear damage, helps the microbial metabolism fermentation; Peripheral in addition liquefied gas content is high, and its density is less than guiding device inner core density of liquid, and this density official post fermented liquid circulation is more smooth and easy.

As shown in Figure 1; Said refrigerating unit comprises first cooling jacket 9 and second cooling jacket 10 of being located at guiding device 3 walls of being located at tank body 1 wall; Said first cooling jacket 9 is arranged on outer wall or the inwall or the inside and outside wall of tank body 1, and said second cooling jacket 10 is arranged on outer wall or the inwall or the inside and outside wall of guiding device 3.Said first cooling jacket 9 and second cooling jacket 10 can adopt flow channel type a or honeycomb fashion b (seeing Fig. 4 a, 4b), are to be connected by welding fabrication of thin-wall stainless steel laser, and the former weld seam is a straight line, and form the zigzag closed channel; Latter's weld seam is discrete point-like, and each solder joint is the point of fixity of chuck, also is the flow-disturbing point of coolant flow, helps to improve heat transfer coefficient.Among the figure; " ⊙ " representes cooling liquid outlet,

represent cooling liquid inlet.Wherein Fig. 4 a is the head and the tail part of cooling jacket, establishes quench liquid in stem and imports and exports, at afterbody quench liquid conversion direction; Fig. 4 b is the part after launch on the cooling jacket cylindrical surface; This kind chuck has material province, big, the weld seam safety advantages of higher of heat interchanging area; Only possibly how to arrange second cooling jacket 10 at guiding device 3 inside and outside walls in addition; Because guiding device 3 inner fermented liquid flow velocitys are greater than outside flow velocity usually; And guiding device 3 wall thickness are thin, thermal resistance is less; Therefore be arranged in big than first cooling jacket 9 on the fermentor tank wall of second cooling jacket, 10 its heat transfer coefficients on the guiding device 3, also promptly can bear bigger cooling heat load by less heat transfer area;

As shown in Figure 1; Said gas barrier comprises escape pipe 6, efficiently revolves and hit gas-liquid separator 5, liquid return tube 7; The top, center that one end of said vapor pipe 4 is arranged on tank body 1 joins with venting port 12, the other end is connected efficiently to revolve and hits gas-liquid separator 5; Said efficiently revolve to hit be connected with escape pipe 6 and liquid return tube 7 on the gas-liquid separator 5, the gas-liquid-solid mixture that is brought by vapor pipe 4 is after separator is handled, the solid, liquid thing of separating passes back into the central inlet place of guiding device 3 in the tank body 1 through liquid return tube 7; Be convenient to that reflux is drawn and with the fermented liquid homogeneous, the gas of separating is discharged by escape pipe 6, regulating valve 8.

Present embodiment only is described with regard to preferred examples; Can not be interpreted as protection domain restriction to the utility model; Depart from some positions, center with what inlet mouth (pipe), venting port (pipe) were located at tank base or top, perhaps guiding device 3 depart from a little tank body 1 hub some, still can obtain the technique effect that similarly protrudes in background technology significantly; Though be not best, also still be that we require protection domain.

Claims

1. eddy flow airlift fermentor; It comprises inlet pipe, the vapor pipe that is provided with on tank body, diffuser, gas barrier, refrigerating unit and the said tank body, and said inlet pipe is connected with diffuser, and said vapor pipe is connected with gas barrier; It is characterized in that: said inlet pipe is located at the mid-way of tank base or near the tank base position; Said vapor pipe is located at the mid-way at tank body top, and said diffuser is a cyclone mixer, is located at jar intravital bottom perhaps near the tank base position; And be connected with inlet pipe; Above cyclone mixer, be provided with guiding device, said guiding device is the tubular structure of both ends open, is on the axis that vertically is arranged on tank body; Said jar of intravital fermentation gas-liquid is the eddy flow state and mixes under the effect of cyclone mixer, and makes inside and outside cyclic motion along guiding device.

2. eddy flow airlift fermentor according to claim 1 is characterized in that said guiding device is divided into several sections that arrange up and down in tank body, and the upper end of each section guiding device forms is convenient to the hole enlargement mouth that fermented liquid flows into.

3. according to claim 1 or 2 described eddy flow airlift fermentors; It is characterized in that said cyclone mixer comprises inner housing and body skin, inner housing top or bottom communicate with inlet pipe, accordingly; The top of the top of body skin and bottom or body skin is provided with fluid inlet; The center of inner housing is circle-shaped some blades that are distributed with, and in inner housing, forms air-flow eddy flow passage, and forms the swirl channel of gas-liquid mixed between inner housing and the body skin.

4. eddy flow airlift fermentor according to claim 1 is characterized in that said refrigerating unit comprises first cooling jacket of being located at the tank body wall and second cooling jacket of being located at the guiding device wall.

5. eddy flow airlift fermentor according to claim 4 is characterized in that said first cooling jacket is arranged on outer wall or the inwall or the inside and outside wall of tank body, and said second cooling jacket is arranged on outer wall or the inwall or the inside and outside wall of guiding device.

6. eddy flow airlift fermentor according to claim 5 is characterized in that said first cooling jacket and second cooling jacket adopt honeycomb fashion or flow channel type, is by welding fabrication of thin-wall stainless steel laser.

7. eddy flow airlift fermentor according to claim 1; It is characterized in that said gas barrier comprises efficiently revolving hits gas-liquid separator, liquid return tube and escape pipe; One end of said vapor pipe inserts the fermentor tank top center, the other end connection is efficiently revolved and hit gas-liquid separator; Be connected with escape pipe and liquid return tube on the said gas-liquid separator; The gas-liquid-solid mixture that is brought by vapor pipe is after separator is handled, and the solid, liquid thing of separating passes back in the tank body through liquid return tube, and the gas of separating is discharged by escape pipe.

8. eddy flow airlift fermentor according to claim 8, the liquid outflow end that it is characterized in that said liquid return tube is located at the ingress of jar intravital guiding device, and is in below the initial liquid level of fermentation.