CN208434676U - A kind of fermentor with machinery and air Double stirring - Google Patents

A kind of fermentor with machinery and air Double stirring Download PDF

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Publication number
CN208434676U
CN208434676U CN201721797630.1U CN201721797630U CN208434676U CN 208434676 U CN208434676 U CN 208434676U CN 201721797630 U CN201721797630 U CN 201721797630U CN 208434676 U CN208434676 U CN 208434676U
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air
tank body
air intake
cover
rotation axis
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CN201721797630.1U
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Chinese (zh)
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朱苾锋
朱景宇
李云玮
朱星宇
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Kunming Sky Red Biological Technology Co Ltd
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Kunming Sky Red Biological Technology Co Ltd
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Abstract

Cover is sealed with mechanical and air Double stirring fermentor, including tank body, motor, several air intake ducts, compressed air hoses, the tank body upper end the utility model discloses a kind of;It is provided with feed inlet and breather valve on the cover, charging end cap is provided on feed inlet;The motor is mounted on the middle part of cover, and the motor passes through shaft coupling and the intracorporal rotation axis connection of tank;The lower sidewall of the tank body is provided with discharge port, and valve is provided on discharge port;One end of the air intake duct is connect with compressed air hose, and the other end passes through cover and extend into tank body;The bottom end of the air intake duct is sealed, and axially disposed there are several fumaroles in the middle and lower part of air intake duct;Several hexagonal turbine stirring leaves are connected in the rotation axis.The air-flow sprayed in fumarole is dispersed into minute bubbles by the hexagonal turbine stirring leaf being arranged in rotation axis, increases gas liquid interfacial area, so that gas-liquid mixed is uniform, dissolved oxygen rate is higher.

Description

A kind of fermentor with machinery and air Double stirring
Technical field
The utility model belongs to installation for fermenting technical field, and in particular to a kind of with mechanical and air Double stirring hair Fermentation tank.
Background technique
Ferment is nickname of the enzyme in Japan and Taiwan, typically refers to ferment the raw materials such as water fruits and vegetables, sugar, Period by glycolysis reaction and enzymatic reaction, greatly improves the enzymatic activity in raw material, and the quantity of enzyme is increased sharply, and ultimately forms to people The beneficial ferment of body.Fruit ferment have help digest, promote metabolism, anti-inflammatory, improve the immunity of the human body, beauty and other effects.
Existing ferment production process, mainly using fruits and vegetables as raw material, by sorting, going handle, cleaning, broken, defibrination, so After ferment, in entire technical process, mostly important is exactly to ferment, and the quality of fermentation directly influences the product of final products Matter.As fermenter volume in the prior art is increasing, the low limiting factor for becoming fermentation process of oxygen rate of dissolution is single Industrial needs are no longer satisfied by traditional mechanical stirring or single air stirring.Existing some fermentors Have to combine mechanical stirring and air stirring and fermentation liquid is stirred, uneven but there is gas-liquid mixeds, oxygen is molten The problems such as rate is lower is solved, greatly affected the process of fermentation and the quality of product.
Utility model content
The purpose of this utility model is to provide a kind of with mechanical and air Double stirring fermentor, it is intended to solve existing Have in technology that fermentor is because gas-liquid mixed is uneven, the lower problem of oxygen rate of dissolution.
In order to solve the above-mentioned technical problem, the technical solution of the utility model are as follows:
A kind of fermentor with machinery and air Double stirring, including tank body, motor, several air intake ducts, pressure Contracting air hose, the tank body upper end are sealed with cover;It is provided with feed inlet and breather valve on the cover, on feed inlet It is provided with charging end cap;The motor is mounted on the middle part of cover, and the motor passes through shaft coupling and the intracorporal rotation axis of tank Connection;The lower sidewall of the tank body is provided with discharge port, and valve is provided on discharge port;One end of the air intake duct It is connect with compressed air hose, the other end passes through cover and extend into tank body;The bottom end of the air intake duct is sealed, and air into The middle and lower part of tracheae is axially disposed several fumaroles;Several hexagonal turbine stirring leaves are connected in the rotation axis.
Further, the air intake duct is four, and four air intake ducts are uniformly divided centered on the rotation axis Cloth is in the tank body.
Further, several groups vertical baffle is provided on the inner sidewall of the tank body, the vertical baffle is perpendicular to tank Body sidewall.
Further, defoaming rake is provided with above the rotation axis top layer hexagonal turbine stirring leaf, defoaming rake is fixed It is connected in the rotation axis.
Further, the fumarole is oblong-shaped, and the width of the fumarole is 0.1mm-5mm, fumarole Length is 10mm-100mm.
The utility model has the beneficial effects that
Traditional mechanical stirring combination air stirring is utilized in the utility model, by the way that the paddle in rotation axis to be arranged For hexagonal turbine stirring leaf, while several fumaroles are offered on air intake duct, hexagonal turbine stirring leaf can be by jet The high pressure sterile air sprayed in hole is dispersed into minute bubbles, increases gas liquid interfacial area, substantially increases being uniformly mixed for gas-liquid The dissolved oxygen rate of degree and filtrated air in fermentation liquid ensure that the quality of product to improve fermentation rate.
Detailed description of the invention
Fig. 1 is the utility model embodiment structural schematic diagram;
Fig. 2 is the utility model hexagonal turbine stirring impeller structure schematic diagram.
In figure, 1- tank body, 2- cover, 3- motor, 4- air intake duct, 5- compressed air hose, 6- feed inlet, 7- breathing Valve, 8- fumarole, 9- shaft coupling, 10- rotation axis, 11- hexagonal turbine stirring leaf, 12- vertical baffle, 13- defoaming rake, 14- go out Material mouth, 15- valve, 16- charging end cap.
Specific embodiment
Specific embodiment of the present utility model is described further with reference to the accompanying drawing.It should be noted that The explanation of these embodiments is used to help to understand the utility model, but does not constitute the restriction to the utility model.This Outside, technical characteristic involved in the various embodiments of the present invention described below is as long as they do not conflict with each other It can be combined with each other.
As shown in Figure 1,
It is a kind of with mechanical and air Double stirring fermentor, including tank body 1, motor 3, several air intake ducts 4, Compressed air hose 5,1 upper end of tank body are sealed with cover 2;Feed inlet 6 and breather valve 7 are provided on cover 2, in feed inlet 6 On be provided with charging end cap 16;The lower sidewall of tank body 1 is provided with discharge port 14, and valve 15 is provided on discharge port 14;It is empty One end of gas air inlet pipe 4 is connect with compressed air hose 5, and the other end passes through cover 2 and extend into tank body 1;Air intake duct 4 Bottom end sealing, and axially disposed there are several fumaroles 8 in the middle and lower part of air intake duct 4;Motor 3 is mounted on the middle part of cover 2, And motor 3 is connect by shaft coupling 9 with the rotation axis 10 in tank body 1, and several hexagonal turbine stirring leaves are connected in rotation axis 10 11.Due to being provided with hexagonal turbine stirring leaf 11 in rotation axis 10, while several fumaroles are offered on air intake duct 4 8, the high pressure sterile air that in fumarole 8 spray can be dispersed into minute bubbles by hexagonal turbine stirring leaf 11, increase gas-liquid contact Area substantially increases rate of dissolution of the oxygen in the mixing uniformity and filtrated air of gas-liquid in fermentation liquid, to mention High fermentation rate.
Specifically, air intake duct 4 is four, four air intake ducts 4 are evenly distributed on tank centered on rotation axis 10 In body 1.Such structure design not only simply, but also increases filtrated air while increasing the supply of filtrated air Distribution area.Rotation axis 10 is driven to rotate by motor 3, so that hexagonal turbine stirring leaf 11 be driven to spray fumarole 8 Gas is cut, so that filtrated air is more uniform in 1 inside gas-liquid mixed of tank body, improves filtrated air in tank body 1 Oxygen rate of dissolution.
Specifically, being provided with several groups vertical baffle 12 on the inner wall of tank body 1, vertical baffle 12 is perpendicular to 1 side wall of tank body. In this way under the action of air-flow when fermentation liquid flows in tank body 1, due to encountering vertical baffle 11, fermentation liquid effectively flows back The mixing of gas and fermentation liquid is further enhanced, so as to further increase fermentation rate.
Specifically, being provided with defoaming rake 13, defoaming rake 13 in the top of 10 top layer's hexagonal turbine stirring leaf 11 of rotation axis It is fixedly connected in rotation axis 10, defoaming rake 13 can reduce foam to fermentation in time by the removal of foam on fermentation liquid surface The influence of process.
Specifically, fumarole 8 is oblong-shaped, and the width of fumarole 8 is 0.1mm-5mm, and the length of fumarole 8 is 10mm-100mm is formed by wire cutting in the fumarole 8 that long wind shape designs, the uniformity of jet can be improved.
The course of work of the utility model: in use, being first shut off 14 valve of discharge port, carrying out feed liquor by feed opening 6, After which after fumarole 8 is flooded in fermentation liquid body fluid position, high pressure sterile air enters air inlet from compressed air hose 5 in tank body 1 In pipe 4, high pressure sterile air is sprayed from fumarole 8 is stirred fermentation liquid, while startup power supply, and motor 3 drives rotation The rotation of axis 10 carries out mechanical stirring to fermentation liquid in tank body 1, and the hexagonal turbine stirring leaf 11 being arranged in rotation axis 10 is by fumarole The high pressure sterile air sprayed in 8 is evenly dispersed to increase gas liquid interfacial area at minute bubbles, improves dissolved oxygen rate;With the use of disappearing Bubble rake 13 can reduce influence of the foam to fermentation process in time by the removal of foam;And more air intake ducts of its setting 4 increase the distribution area of filtrated air while increasing the supply of filtrated air, and then stir in each layer hexagonal turbine It mixes and improves dissolved oxygen efficiency under the action of leaf 11.
The embodiments of the present invention is explained in detail in conjunction with attached drawing above, but the utility model is not limited to be retouched The embodiment stated.For a person skilled in the art, right in the case where not departing from the utility model principle and spirit These embodiments carry out a variety of change, modification, replacement and modification, still fall in the protection scope of the utility model.

Claims (5)

1. a kind of with mechanical and air Double stirring fermentor, including tank body (1), motor (3), several air intake ducts (4), compressed air hose (5), tank body (1) upper end are sealed with cover (2);Feed inlet is provided on the cover (2) (6) and breather valve (7) charging end cap (16), are provided on feed inlet (6);The motor (3) is mounted in cover (2) Portion, and the motor (3) is connect by shaft coupling (9) with the rotation axis (10) in tank body (1);Under the side wall of the tank body (1) Portion is provided with discharge port (14), and valve (15) are provided on discharge port (14);One end of the air intake duct (4) and compression Air hose (5) connection, the other end pass through cover (2) and extend into tank body (1);It is characterized by: the air intake duct (4) Bottom end sealing, and the middle and lower part of air intake duct (4) axially disposed has several fumaroles (8);Connect on the rotation axis (10) It is connected to several hexagonal turbine stirring leaves (11).
2. according to claim 1 a kind of with mechanical and air Double stirring fermentor, it is characterised in that: the sky Gas air inlet pipe (4) is four, and four air intake ducts (4) are evenly distributed on the tank body centered on the rotation axis (10) (1) in.
3. according to claim 1 a kind of with mechanical and air Double stirring fermentor, it is characterised in that: the tank It is provided on the inner sidewall of body (1) several groups vertical baffle (12), the vertical baffle (12) is perpendicular to tank body (1) side wall.
4. according to claim 1 a kind of with mechanical and air Double stirring fermentor, it is characterised in that: described turn Defoaming rake (13) is provided with above moving axis (10) top layer's hexagonal turbine stirring leaf (11), defoaming rake (13) is fixedly connected on institute It states on rotation axis (10).
5. according to any one of claim 1 to 4 a kind of with mechanical and air Double stirring fermentor, feature Be: the fumarole (8) is oblong-shaped, and the width of the fumarole (8) is 0.1mm-5mm, the length of fumarole (8) For 10mm-100mm.
CN201721797630.1U 2017-12-21 2017-12-21 A kind of fermentor with machinery and air Double stirring Active CN208434676U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721797630.1U CN208434676U (en) 2017-12-21 2017-12-21 A kind of fermentor with machinery and air Double stirring

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721797630.1U CN208434676U (en) 2017-12-21 2017-12-21 A kind of fermentor with machinery and air Double stirring

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CN208434676U true CN208434676U (en) 2019-01-29

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115558579A (en) * 2022-11-14 2023-01-03 江苏尚昆生物设备有限公司 Fermentation equipment
CN116162527A (en) * 2023-02-27 2023-05-26 河北首朗新能源科技有限公司 Fermentation reactor
WO2023108311A1 (en) * 2021-12-13 2023-06-22 山西农业大学山西功能食品研究院 Fruit and vegetable enzyme fermentation equipment for maintaining biological activity

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023108311A1 (en) * 2021-12-13 2023-06-22 山西农业大学山西功能食品研究院 Fruit and vegetable enzyme fermentation equipment for maintaining biological activity
CN115558579A (en) * 2022-11-14 2023-01-03 江苏尚昆生物设备有限公司 Fermentation equipment
CN115558579B (en) * 2022-11-14 2023-10-31 江苏尚昆生物设备有限公司 Fermentation equipment
CN116162527A (en) * 2023-02-27 2023-05-26 河北首朗新能源科技有限公司 Fermentation reactor

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