Refined parallel fermentation tank of two cracked yeast broken wall crude extract

文档序号:1932484 发布日期:2021-12-07 浏览:14次 中文

阅读说明:本技术 一种二裂酵母破壁粗提液的精制平行发酵罐 (Refined parallel fermentation tank of two cracked yeast broken wall crude extract ) 是由 蒋清昀 杨国军 于 2021-10-14 设计创作,主要内容包括:本发明提供了一种二裂酵母破壁粗提液的精制平行发酵罐,涉及布料清洁技术领域,包括:发酵罐;所述发酵罐由顶盖和罐体构成,顶盖连接在罐体顶部,顶盖顶部开设有进料口,罐体底部开设有排料口;所述发酵罐外部套装有保温层,且发酵罐顶部安装有电机,电机的驱动轴上安装有搅拌轴,搅拌轴位于发酵罐内部,搅拌轴外侧设有三组搅拌叶。本发明能够在发酵罐内部初始温度过低时,通过加热器对发酵罐内部原料加热效果,使发酵罐内部原料能够在短时间内升温至发酵适宜温度,提升发酵罐内部原料发酵效率。解决了传统发酵罐在初始发酵时,发酵罐内部微生物受低温影响难以迅速繁殖,影响原料发酵效率的问题。(The invention provides a refined parallel fermentation tank of secondary-cracking yeast wall-breaking crude extract, which relates to the technical field of cloth cleaning and comprises the following components: a fermentation tank; the fermentation tank consists of a top cover and a tank body, the top cover is connected to the top of the tank body, the top of the top cover is provided with a feed inlet, and the bottom of the tank body is provided with a discharge outlet; the fermentation cylinder outside cover is equipped with the heat preservation, and the fermentation cylinder top installs the motor, installs the (mixing) shaft in the drive shaft of motor, and the (mixing) shaft is located the fermentation cylinder inside, and the (mixing) shaft outside is equipped with three stirring leaves of group. According to the invention, when the initial temperature in the fermentation tank is too low, the raw materials in the fermentation tank can be heated to the proper fermentation temperature in a short time through the heating effect of the heater, so that the fermentation efficiency of the raw materials in the fermentation tank is improved. The problem of traditional fermentation cylinder when initial fermentation, the inside microorganism of fermentation cylinder receives low temperature to influence and is difficult to breed rapidly, influences raw materials fermentation efficiency is solved.)

1. The utility model provides a refined parallel fermentation cylinder of two cracked yeast broken wall crude extract which characterized in that includes: a fermentation tank (1);

the fermentation tank (1) is composed of a top cover (101) and a tank body (102), the top cover (101) is connected to the top of the tank body (102), a feed inlet (1011) is formed in the top of the top cover (101), and a discharge outlet (1021) is formed in the bottom of the tank body (102);

the heat-insulating layer (2) is sleeved outside the fermentation tank (1), the motor (3) is installed at the top of the fermentation tank (1), the stirring shaft (4) is installed on the driving shaft of the motor (3), the stirring shaft (4) is located inside the fermentation tank (1), and three groups of stirring blades (401) are arranged on the outer side of the stirring shaft (4);

fermentation cylinder (1) outside is connected with circulating pump (5), and circulating pump (5) are linked together with electromagnetic switching valve (6) to electromagnetic switching valve (6) are linked together with heater (7) and cooling tube (8) respectively, and cooling tube (8) are connected in heat preservation (2) outside.

2. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: the heat exchange channel (1022) is circumferentially arranged in the wall of the tank body (102), the heat exchange channel (1022) is vertically meandered, and the inner side of the tank body (102) is circumferentially welded with heat conducting fins (1023).

3. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: the electromagnetic switching valve (6) is provided with a liquid outlet (601), a liquid inlet (602), a hot inlet (603), a cold inlet (604), a hot outlet (605) and a cold outlet (606) on the outer side respectively, the liquid outlet (601) is communicated with the hot inlet (603) and the cold inlet (604) respectively, and the liquid inlet (602) is communicated with the hot outlet (605) and the cold outlet (606) respectively.

4. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 2, wherein: the liquid inlet end of the heat exchange channel (1022) is communicated with the circulating pump (5), the liquid outlet end of the heat exchange channel (1022) is communicated with the liquid inlet (602) of the electromagnetic switching valve (6), and the circulating pump (5) is communicated with the liquid outlet (601) of the electromagnetic switching valve (6).

5. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: and the liquid discharge end of the heater (7) is communicated with a hot inlet (603) of the electromagnetic switching valve (6), and the liquid inlet end of the heater (7) is communicated with a hot discharge port (605) of the electromagnetic switching valve (6).

6. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: the liquid discharge end of the radiating pipe (8) is communicated with the cold inlet (604) of the electromagnetic switching valve (6), and the liquid inlet end of the radiating pipe (8) is communicated with the cold discharge port (606) of the electromagnetic switching valve (6).

7. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: the radiating pipe (8) is located the fermentation cylinder (1) outside around the form, and the equidistance welding in radiating pipe (8) outside has fin (801).

8. The refined parallel fermentation tank of the crude secondary split yeast wall-breaking extract as claimed in claim 1, wherein: the inner side of the top cover (101) is provided with a cleaning pipe (9), the bottom side of the cleaning pipe (9) is provided with a surrounding spray head (11), the spray head (11) is inclined towards the inner side of the tank body (102), and the cleaning pipe (9) is communicated with a water supply pipeline through a control valve (10).

Technical Field

The invention relates to the technical field of fermentation tanks, in particular to a refined parallel fermentation tank for secondary cracking yeast wall-broken crude extract.

Background

In recent years, the technology and equipment level of Chinese biological fermentation technology have been advanced greatly, and in biological fermentation, a fermentation tank is usually adopted, and the fermentation tank is an external environment device for the growth, propagation and product formation of microorganisms in the fermentation process, replaces the traditional fermentation container, and plays an important role in continuous mass production and yield improvement.

However, in the conventional fermentation tank, the initial temperature inside the fermentation tank is low during the fermentation application process, and the temperature generated by fermentation is generally increased gradually, so that the time for increasing the temperature is long, and during the initial fermentation, microorganisms inside the fermentation tank are affected by low temperature and are difficult to propagate rapidly, which particularly affects the fermentation efficiency of raw materials.

Disclosure of Invention

In view of the above, the invention provides a refined parallel fermentation tank for a secondary cracking yeast wall-broken crude extract, which can move a valve core in an electromagnetic switching valve downwards when the initial temperature in the fermentation tank is too low, so that a liquid outlet is communicated with a heat inlet, a liquid inlet is communicated with a heat outlet, a circulating pump conveys heat exchange liquid in a heat exchange channel into a heater, and the heat exchange liquid is heated by the heater, so that the effect of heating raw materials in the fermentation tank is achieved, the raw materials in the fermentation tank can be heated to a proper fermentation temperature in a short time, and the fermentation efficiency of the raw materials in the fermentation tank is improved.

The invention provides a refined parallel fermentation tank for a secondary cracking yeast wall-breaking crude extract, which specifically comprises the following steps: a fermentation tank;

the fermentation tank consists of a top cover and a tank body, the top cover is connected to the top of the tank body, the top of the top cover is provided with a feed inlet, and the bottom of the tank body is provided with a discharge outlet;

the fermentation tank is sleeved with a heat insulation layer, the top of the fermentation tank is provided with a motor, a driving shaft of the motor is provided with a stirring shaft, the stirring shaft is positioned in the fermentation tank, and three groups of stirring blades are arranged outside the stirring shaft;

the fermentation cylinder outside is connected with the circulating pump, and the circulating pump is linked together with the electromagnetism diverter valve to the electromagnetism diverter valve is linked together with heater and cooling tube respectively, and the cooling tube is connected in the heat preservation outside.

Optionally, a heat exchange channel is circumferentially arranged in the tank wall of the tank body, the heat exchange channel is vertically meandered, and the inner side of the tank body is circumferentially welded with heat conducting fins.

Optionally, a liquid discharge port, a liquid inlet, a hot inlet, a cold inlet, a hot discharge port and a cold discharge port are respectively formed in the outer side of the electromagnetic switching valve, the liquid discharge port is respectively communicated with the hot inlet and the cold inlet, and the liquid inlet is respectively communicated with the hot discharge port and the cold discharge port.

Optionally, a liquid inlet end of the heat exchange channel is communicated with a circulating pump, a liquid discharge end of the heat exchange channel is communicated with a liquid inlet of the electromagnetic switching valve, and the circulating pump is communicated with a liquid discharge port of the electromagnetic switching valve.

Optionally, the heater liquid discharge end is communicated with a hot inlet of the electromagnetic switching valve, and the heater liquid inlet end is communicated with a hot outlet of the electromagnetic switching valve.

Optionally, the liquid discharge end of the heat dissipation pipe is communicated with the cold inlet of the electromagnetic switching valve, and the liquid inlet end of the heat dissipation pipe is communicated with the cold discharge port of the electromagnetic switching valve.

Optionally, the cooling tube is located the fermentation cylinder outside in the form of encircleing, and the welding of cooling tube outside equidistance has the fin.

Optionally, a cleaning pipe is installed on the inner side of the top cover, a spray head is installed on the bottom side of the cleaning pipe in a surrounding manner, the spray head faces the inner side of the tank body in an inclined manner, and the cleaning pipe is communicated with the water supply pipeline through a control valve.

Advantageous effects

According to the refined parallel fermentation tank of the secondary cracking yeast wall-broken crude extract, compared with the traditional fermentation tank, when the initial temperature in the fermentation tank is too low, the valve core in the electromagnetic switching valve moves downwards, the liquid outlet is communicated with the heat inlet, the liquid inlet is communicated with the heat outlet, the circulating pump conveys the heat exchange liquid in the heat exchange channel into the heater, the heat exchange liquid is heated by the heater, the effect of heating the raw materials in the fermentation tank is achieved, the raw materials in the fermentation tank can be heated to the proper fermentation temperature in a short time, and the fermentation efficiency of the raw materials in the fermentation tank is improved.

In addition, through the setting of the internal portion heat transfer passageway of jar, when the inside temperature of fermentation cylinder is higher than or is less than the required temperature of fermentation, heat transfer liquid through the inside circulation of heat transfer passageway heaies up or cools down to the inside raw materials of fermentation cylinder, makes the inside fermentation temperature of fermentation cylinder keep more than 20 degrees centigrade below 30, conducting strip increase raw materials and jar internal wall area of contact promote the inside heat exchange efficiency of fermentation cylinder, makes the inside suitable fermentation temperature that keeps of fermentation cylinder, the inside raw materials fermentation effect of guarantee fermentation cylinder.

In addition, through the setting of electromagnetic switch valve and cooling tube, when the inside temperature of fermentation cylinder is higher than the fermentation suitable temperature, the inside case rebound of electromagnetic switch valve, make the leakage fluid dram and cold import be linked together, the inlet is linked together with cold leakage fluid dram, the circulating pump is carried the inside heat transfer liquid of heat transfer passageway to the cooling tube in, release the air with the inside heat that carries of heat transfer liquid through the cooling tube, play the inside raw materials cooling effect of fermentation cylinder, make the inside raw materials of fermentation cylinder can cool down to the fermentation suitable temperature in the short time, the inside raw materials fermentation effect of guarantee fermentation cylinder.

In addition, through the setting of clean pipe and shower nozzle, after the fermentation of the inside raw materials of fermentation cylinder finishes the exhaust, wash the cleanness to the adnexed remaining raw materials of jar internal wall through the shower nozzle, make remaining raw materials discharge through the bin outlet, avoid remaining raw materials rotten inside the fermentation cylinder, cause the pollution to follow-up raw materials fermentation.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings of the embodiments will be briefly described below.

The drawings in the following description relate to some embodiments of the invention only and are not intended to limit the invention.

In the drawings:

FIG. 1 shows a schematic axial side view of an embodiment according to the invention;

FIG. 2 is a cross-sectional view of the exterior insulation of the fermenter according to an embodiment of the present invention;

FIG. 3 shows a schematic view of a cutaway inside a fermenter according to an embodiment of the present invention;

FIG. 4 shows a schematic diagram of a top cover isometric configuration according to an embodiment of the present invention;

FIG. 5 is a schematic diagram showing a connection structure of an electromagnetic switching valve and a heater according to an embodiment of the present invention;

FIG. 6 is a schematic view illustrating a connection structure of the electromagnetic switch valve and the radiating pipe according to an embodiment of the present invention;

figure 7 is a schematic diagram illustrating an axial side construction of a radiating pipe according to an embodiment of the present invention;

fig. 8 shows a cross-sectional structural schematic diagram of the electromagnetic switching valve according to the embodiment of the invention.

List of reference numerals

1. A fermentation tank; 101. a top cover; 1011. a feed inlet; 102. a tank body; 1021. a discharge outlet; 1022. a heat exchange channel; 1023. a heat conductive sheet;

2. a heat-insulating layer;

3. a motor;

4. a stirring shaft; 401. stirring blades;

5. a circulation pump;

6. an electromagnetic switching valve; 601. a liquid discharge port; 602. a liquid inlet; 603. a hot inlet; 604. a cold inlet; 605. a hot exhaust port; 606. a cold discharge port;

7. a heater;

8. a radiating pipe; 801. a heat sink;

9. cleaning the tube;

10. a control valve;

11. and (4) a spray head.

Detailed Description

In order to make the objects, aspects and advantages of the embodiments of the present invention more apparent, the embodiments of the present invention will be described in detail with reference to the accompanying drawings. Unless otherwise indicated, terms used herein have the ordinary meaning in the art. Like reference symbols in the various drawings indicate like elements.

The first embodiment is as follows:

please refer to fig. 1 to 8:

the invention provides a refined parallel fermentation tank of a secondary cracking yeast wall breaking crude extract, which comprises: a fermentation tank 1;

the fermentation tank 1 is composed of a top cover 101 and a tank body 102, wherein the top cover 101 is connected to the top of the tank body 102, the top of the top cover 101 is provided with a feed inlet 1011, and the bottom of the tank body 102 is provided with a discharge outlet 1021;

the heat preservation layer 2 is sleeved outside the fermentation tank 1, the motor 3 is installed at the top of the fermentation tank 1, the stirring shaft 4 is installed on the driving shaft of the motor 3, the stirring shaft 4 is located inside the fermentation tank 1, and three groups of stirring blades 401 are arranged outside the stirring shaft 4;

the outer side of the fermentation tank 1 is connected with a circulating pump 5, the circulating pump 5 is communicated with an electromagnetic switching valve 6, the electromagnetic switching valve 6 is respectively communicated with a heater 7 and a radiating pipe 8, and the radiating pipe 8 is connected to the outer side of the heat preservation layer 2;

a liquid outlet 601, a liquid inlet 602, a hot inlet 603, a cold inlet 604, a hot outlet 605 and a cold outlet 606 are respectively formed in the outer side of the electromagnetic switching valve 6, the liquid outlet 601 is respectively communicated with the hot inlet 603 and the cold inlet 604, and the liquid inlet 602 is respectively communicated with the hot outlet 605 and the cold outlet 606;

the cooling tube 8 is that the form of encircleing is located the fermentation cylinder 1 outside, and 8 outside equidistance welding of cooling tube have fin 801, and 8 circulation routes of extension cooling tube increase 8 outside heat radiating area of cooling tube through fin 801 to promote the cooling tube 8 to heat exchange liquid cooling effect, the guarantee heat exchange liquid is to the inside raw materials cooling effect of fermentation cylinder 1.

In addition, according to the embodiment of the present invention, a heat exchange channel 1022 is circumferentially opened in the tank wall of the tank 102, the heat exchange channel 1022 is vertically meandered, and a heat conducting sheet 1023 is circumferentially welded on the inner side of the tank 102, a liquid inlet end of the heat exchange channel 1022 is communicated with the circulation pump 5, a liquid outlet end of the heat exchange channel 1022 is communicated with the liquid inlet 602 of the electromagnetic switching valve 6, and the circulation pump 5 is communicated with the liquid outlet 601 of the electromagnetic switching valve 6;

adopt above-mentioned technical scheme, when 1 inside temperature of fermentation cylinder is higher than or is less than the required temperature of fermentation, heat-transfer liquid through the inside circulation of heat transfer passageway 1022 heaies up or cools down to 1 inside raw materials of fermentation cylinder, and conducting strip 1023 increases raw materials and jar body 102 inner wall area of contact, promotes 1 inside heat exchange efficiency of fermentation cylinder, makes 1 inside fermentation temperature that keeps suitable of fermentation cylinder, the inside raw materials fermentation effect of guarantee fermentation cylinder 1.

Further, according to the embodiment of the present invention, the liquid discharge end of the heater 7 communicates with the hot inlet 603 of the electromagnetic switching valve 6, and the liquid inlet end of the heater 7 communicates with the hot outlet 605 of the electromagnetic switching valve 6;

adopt above-mentioned technical scheme, when the inside initial temperature of fermentation cylinder 1 was crossed lowly, the inside case of electromagnetic switch valve 6 moves down, make leakage fluid dram 601 and hot import 603 be linked together, inlet 602 is linked together with hot exhaust 605, circulating pump 5 carries the inside heat transfer liquid of heat transfer passageway 1022 to heater 7 in, heat transfer liquid heaies up through heater 7, play the heating effect to the inside raw materials of fermentation cylinder 1, make the inside raw materials of fermentation cylinder 1 can heat up to the suitable temperature of fermentation in the short time, promote the inside raw materials fermentation efficiency of fermentation cylinder 1.

In addition, according to the embodiment of the present invention, the liquid discharge end of the heat dissipation pipe 8 communicates with the cold inlet 604 of the electromagnetic switch valve 6, and the liquid inlet end of the heat dissipation pipe 8 communicates with the cold discharge port 606 of the electromagnetic switch valve 6;

adopt above-mentioned technical scheme, when 1 inside temperature of fermentation cylinder is higher than the fermentation suitable temperature, 6 inside case rebound of electromagnetism diverter valve, make leakage fluid dram 601 and cold import 604 be linked together, inlet 602 is linked together with cold discharge port 606, circulating pump 5 carries the inside heat transfer liquid of heat transfer passageway 1022 to in the cooling tube 8, release the air with the inside heat that carries of heat transfer liquid through cooling tube 8, play the effect of cooling to 1 inside raw materials of fermentation cylinder, make 1 inside raw materials of fermentation cylinder can cool down to the fermentation suitable temperature in the short time, the inside raw materials fermentation effect of guarantee fermentation cylinder 1.

Example two:

the inner side of the top cover 101 is provided with a cleaning pipe 9, the bottom side of the cleaning pipe 9 is provided with a spray head 11 in a surrounding manner, the spray head 11 faces the inner side of the tank body 102 in an inclined manner, and the cleaning pipe 9 is communicated with a water supply pipeline through a control valve 10;

adopt above-mentioned technical scheme, after fermentation of the inside raw materials of fermentation cylinder 1 finishes the exhaust, wash the cleanness through shower nozzle 11 to the adnexed remaining raw materials of jar body 102 inner wall, make remaining raw materials discharge through bin outlet 1021, avoid remaining raw materials rotten in fermentation cylinder 1 is inside, cause the pollution to follow-up raw materials fermentation.

The specific use mode and function of the embodiment are as follows: when the fermentation tank is used, raw materials enter the fermentation tank 1 through the feed inlet 1011, the motor 3 drives the stirring shaft 4 to rotate, and the raw materials are mixed and stirred through the stirring blade 401 outside the stirring shaft 4; when the initial temperature in the fermentation tank 1 is low, the valve core in the electromagnetic switching valve 6 moves downwards to enable the liquid outlet 601 to be communicated with the heat inlet 603, the liquid inlet 602 to be communicated with the heat outlet 605, the circulating pump 5 conveys the heat exchange liquid in the heat exchange channel 1022 to the heater 7, the heat exchange liquid is heated by the heater 7, the heat exchange liquid circulating in the heat exchange channel 1022 heats the raw material in the fermentation tank 1, the raw material in the fermentation tank 1 can be heated to the proper fermentation temperature in a short time, and the fermentation efficiency of the raw material in the fermentation tank 1 is improved; when the internal temperature of the fermentation tank 1 is higher than the proper fermentation temperature, the valve core in the electromagnetic switching valve 6 moves upwards to enable the liquid outlet 601 to be communicated with the cold inlet 604, the liquid inlet 602 is communicated with the cold outlet 606, the circulating pump 5 conveys the heat exchange liquid in the heat exchange channel 1022 to the radiating pipe 8, and the heat carried in the heat exchange liquid is released into the air through the radiating pipe 8, so that the cooling effect on the raw materials in the fermentation tank 1 is achieved, the raw materials in the fermentation tank 1 can be cooled to the proper fermentation temperature in a short time, and the fermentation effect of the raw materials in the fermentation tank 1 is guaranteed; after the fermentation of the raw materials in the fermentation tank 1 is finished and the raw materials are completely discharged from the discharge opening 1021, the residual raw materials attached to the inner wall of the tank body 102 are washed and cleaned through the spray head 11, so that the residual raw materials are discharged through the discharge opening 1021, and the phenomenon that the residual raw materials are deteriorated in the fermentation tank 1 and cause pollution to subsequent raw material fermentation is avoided.

Finally, it should be noted that, when describing the positions of the components and the matching relationship therebetween, the present invention is usually illustrated by one/a pair of components, however, it should be understood by those skilled in the art that such positions, matching relationship, etc. are also applicable to other/other pairs of components.

The above description is intended to be illustrative of the present invention and not to limit the scope of the invention, which is defined by the claims appended hereto.

14页详细技术资料下载
上一篇:一种医用注射器针头装配设备
下一篇:一种微生物处理的米线加工方法及设备

网友询问留言

已有0条留言

还没有人留言评论。精彩留言会获得点赞!

精彩留言,会给你点赞!