CN101294126B - Liquid dynamic surface fermentation tower - Google Patents
Liquid dynamic surface fermentation tower Download PDFInfo
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- CN101294126B CN101294126B CN2008101224413A CN200810122441A CN101294126B CN 101294126 B CN101294126 B CN 101294126B CN 2008101224413 A CN2008101224413 A CN 2008101224413A CN 200810122441 A CN200810122441 A CN 200810122441A CN 101294126 B CN101294126 B CN 101294126B
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Abstract
The invention discloses a liquid dynamic surface fermenting tower. A top cover (2) is arranged on a tower body (1) to form a cylindrical fermenting tower; two support posts (3) vertical to the tower bottom are arranged on both ends of the fermenting tower in the diameter direction; two lifting chains (5) in cross arrangement with the support posts (3) are arranged in the fermenting tower; a group of shafts (4) are horizontally and movably arranged on the support posts (3) hierarchically; segmental liquid receiving disks (6) are arranged on the shafts (4); the arc vertexes of the segmental liquid receiving disks (6) are connected with the lifting chains (5) through chain rings (14); and the round notches of the liquid receiving disks are alternately arranged in reverse direction. The invention is a continuous fermenting device between surface standing fermentation and liquid-state subsurface fermentation. The liquid keeps sufficient contact with the air in the tower by arranging the liquid dynamic surface, and the liquid temperature can be transferred fast and uniformly through circulation, thus shortening fermentation period and improving fermentation efficiency.
Description
Technical field
The present invention relates to a kind of microbial liquid fermentation unit, be specifically related to a kind of liquid dynamic surface fermentation tower, can be applicable to liquid phase process production, flavouring of vinegar (fruit vinegar), soy sauce, fruit wine and other fermented drinks etc.
Background technology
There is long biofermentation technique in China, and zymotechnique mainly contains solid-state and liquid two big classes.For solid-state, liquid fermentation method is short because of its fermentation period, plant factor is high, fermentation yield advantages of higher obtains extensive studies and utilization.With regard to liquid fermentings such as vinegar, soy sauce, at present report mostly is surperficial standing for fermentation method and liquid submerged fermentation method.Surface standing for fermentation traditional method owned by France, though simple, the production cycle is long, and occupation area of equipment is big, and raw material availability is low, unstable product quality; Though deep liquid fermentation process is advanced, to bacterial classification and manufacturing requirements height, main equipment and utility appliance system are huge, the equipment one-time investment is big, throughput change space degree of regulation is low, the process cost height, and the versatility of equipment, dexterity, turndown ratio are poor.
Summary of the invention
The objective of the invention is to: a kind of liquid dynamic surface fermentation tower is provided, be the continuously ferment device of boundary between surperficial standing for fermentation and liquid submerged fermentation, by founding liquid dynamic surface, make liquid fully contact with the Ta Nei air, simultaneously by flowing, it is quick, balanced to make that the fluid temperature transmission is able to, and shortens fermentation period, improves fermentation efficiency.
The technical solution adopted for the present invention to solve the technical problems is: this fermentation tower comprises tower body, top cover, pillar stiffener, rotating shaft, elevating chain and circle lack the shape liquid dish, top cover is installed on the tower body is constituted the round shape fermentation tower, be positioned at the pillar stiffener at the bottom of two vertical towers are installed at the diametric(al) two ends in the fermentation tower, two elevating chains of installation and pillar stiffener are cross arrangement in fermentation tower, one group of rotating shaft layering horizontal anomalous movement is installed on the pillar stiffener, circle is installed in the rotating shaft is lacked the shape liquid dish, the place, circular arc summit that circle lacks the shape liquid dish connects elevating chain by chain link, and the round breach that circle lacks the shape liquid dish is alternately reversed arrangement; Described circle lacks the shape liquid dish and is made up of scarce shape chassis of circle and cofferdam, the cofferdam is installed on the outer on the scarce shape chassis of circle constitutes the round shape liquid dish that lacks.
In the liquid dynamic surface fermentation tower of the present invention, it is lower than the height in arc cofferdam that circle lacks the round breach cofferdam of shape liquid dish.
In the liquid dynamic surface fermentation tower of the present invention, round breach cofferdam and chassis that circle lacks the shape liquid dish are 100-120 ° of inclination angle.
In the liquid dynamic surface fermentation tower of the present invention, L shaped feed-pipe is installed on the top cover is stretched in the tower to the scarce shape liquid dish of the first layer circle.
In the liquid dynamic surface fermentation tower of the present invention, at the discharge nozzle of the bottom of tower body mounting strap bleeder valve.
In the liquid dynamic surface fermentation tower of the present invention, the round indentation, there that lacks the shape liquid dish at circle is installed the scarce shape liquid dish of software drainage part to lower floor circle.
In the liquid dynamic surface fermentation tower of the present invention, two support bars and rotating shaft formation triangular supports are installed in the bottom that lacks the shape liquid dish at circle, and wherein an end points is positioned at the center of garden breach.
During use, treat that fermented liq enters in the tower in the first layer liquid dish by L type feed-pipe, when liquid surpass the liquid dish circle lack the shape cofferdam height after the overflow of software drainage part water conservancy diversion flow into down in one deck liquid dish, the S-shaped flow direction when liquid of last layer liquid dish is flowed through down one deck liquid dish successively, the fermented liquid that dams in the liquid dish constantly carries out the interval exchange with the main body fermented liquid, makes that the fermented liquid in the liquid dish is brought in constant renewal in.
Actually operating time-division three phases carries out: 1, the cleaning and sterilization stage, and make circle lack the shape liquid dish by elevating chain and tilt around the shaft alternately, material discharges fully in the liquid dish, adopts steam and hot water all can carry out cleaning and sterilization as thermal source; 2, the liquid fermenting stage, this moment, each liquid dish was parallel to stack, and dam liquid and main body fermented liquid are brought in constant renewal in; 3, the fermentation end of a period discharging stage, liquid dish divides two angles to tilt, and is 15 ° and 30 °, is 15 ° when tilting, and liquid discharge is about 2/3rds in the liquid dish, and remaining liq is inoculated with newly advancing material, carries out next step fermentation; When being 30 ° of inclinations, producing fully and finish, liquid discharge finishes.
The invention has the beneficial effects as follows, lack the design of shape liquid dish and the also flexible lifting of process chain of the interfolded between the liquid dish up and down by the garden, this tower is easy to realize dynamically controlling of liquid-flow in process of production, liquid has formed dynamic surface when flowing between liquid dish, flowing fluid constantly contacts with air in the tower, increase the dissolved oxygen content of liquid, improved fermenting speed and the feed stock conversion of microorganism.Simultaneously, software drainage part reduces impact and noise.The present invention has overcome the problem that surperficial standing for fermentation method oxygen supply deficiency, fermentation period are long, fermentation rate is not high, has reduced air-purification unit and the whipping device in the deep liquid fermentation process again.This fermentation tower floor space is little, the fermentation rate height, and turndown ratio is big, dynamic stability, the cycle is short, and process cost is low, invest for a short time, and versatility, dexterity are good, the vinegar (fruit vinegar) of especially suitable medium-sized and small enterprises, soy sauce, drinks (fruit wine) production, flavouring etc.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the schematic cross-section of Fig. 1.
Fig. 3 is Fig. 2 liquid dish synoptic diagram.
Fig. 4 is Fig. 1 fermentation tower production status figure.
Fig. 5 is Fig. 1 fermentation tower discharging state graph.
Fig. 6 is the state graph of Fig. 1 fermentation tower cleaning and sterilizing.
Among the figure: 1 tower body, 2 top covers, 3 pillar stiffeners, 4 rotating shafts, 5 elevating chains, 6 circles lack the shape liquid dish, and 7 circles lack the shape chassis, 8 cofferdam, 9L shape feed-pipe, 10 bleeder valves, 11 discharge nozzles, 12 circle breach cofferdam, 13 software position of splitter, 14 chain links, 15 support bars, 16 circular arc cofferdam.
Embodiment
The present invention is further described below in conjunction with drawings and Examples.
As Figure 1-3, this fermentation tower comprises tower body 1, top cover 2, pillar stiffener 3, carrier 4, elevating chain 5 and circle lack shape liquid dish 6, top cover 2 is installed on the tower body 1 is constituted the round shape fermentation tower, be positioned at the pillar stiffener 3 at the bottom of two vertical towers are installed at the diametric(al) two ends in the fermentation tower, two elevating chains 5 are installed in fermentation tower are cross arrangement with pillar stiffener 3, one group of rotating shaft 4 layering horizontal anomalous movement is installed on the pillar stiffener 3, circle is installed in the rotating shaft 4 is lacked shape liquid dish 6, the place, circular arc summit that circle lacks shape liquid dish 6 connects elevating chain 5 by chain link 14, and the round breach that circle lacks shape liquid dish 6 is alternately reversed arrangement; Described circle lacks shape liquid dish 6 and is made up of scarce shape chassis 7 of circle and cofferdam 8, cofferdam 8 is installed on the outer on the scarce shape chassis 7 of circle constitutes the round shape liquid dish 6 that lacks.
In the liquid dynamic surface fermentation tower of the present invention, it is lower than the height in circular arc cofferdam 16 that circle lacks the round breach cofferdam 12 of shape liquid dish 6.
In the liquid dynamic surface fermentation tower of the present invention, the round breach cofferdam 12 that circle lacks shape liquid dish 6 is 100-120 ° of inclination angle with chassis 7.
In the liquid dynamic surface fermentation tower of the present invention, L shaped feed-pipe 9 is installed on the top cover 2 is stretched in the tower to the scarce shape liquid dish of the first layer circle.
In the liquid dynamic surface fermentation tower of the present invention, at the discharge nozzle 11 of the bottom of tower body 1 mounting strap bleeder valve 10.
In the liquid dynamic surface fermentation tower of the present invention, the round indentation, there that lacks shape liquid dish 6 at circle is installed the scarce shape liquid dish of software drainage part 13 to one lower floors circle.
In the liquid dynamic surface fermentation tower of the present invention, two support bars 15 and rotating shaft 4 formation triangular supports are installed in the bottom that lacks shape liquid dish 6 at circle, and wherein an end points is positioned at the center in breach cofferdam, garden 12.
During use, treat that fermented liq enters in the tower in the first layer liquid dish by L type feed-pipe 9, when liquid surpass the liquid dish circle lack the shape cofferdam height after the overflow of software drainage part water conservancy diversion flow into down in one deck liquid dish, the S-shaped flow direction when liquid of last layer liquid dish is flowed through down one deck liquid dish successively, the fermented liquid that dams in the liquid dish constantly carries out the interval exchange with the main body fermented liquid, makes that the fermented liquid in the liquid dish is brought in constant renewal in.
Actually operating time-division three phases carries out: shown in Fig. 4-6, and 1, the cleaning and sterilization stage, make circle lack the shape liquid dish by elevating chain and tilt around the shaft alternately, material discharges fully in the liquid dish, adopts steam and hot water all can carry out cleaning and sterilization as thermal source; 2, the liquid fermenting stage, this moment, each liquid dish was parallel to stack, and dam liquid and main body fermented liquid are brought in constant renewal in; 3, the fermentation end of a period discharging stage, liquid dish divides two angles to tilt, and is 15 ° and 30 °, is 15 ° when tilting, and liquid discharge is about 2/3rds in the liquid dish, and remaining liq is inoculated with newly advancing material, carries out next step fermentation; When being 30 ° of inclinations, producing fully and finish, liquid discharge finishes.
Claims (5)
1. liquid dynamic surface fermentation tower, it is characterized in that: this fermentation tower comprises tower body (1), top cover (2), pillar stiffener (3), carrier (4), elevating chain (5) and circle lack shape liquid dish (6), tower body (1) is gone up top cover (2) formation round shape fermentation tower is installed, be positioned at the pillar stiffener (3) at the bottom of two vertical towers are installed at the diametric(al) two ends in the fermentation tower, two elevating chains (5) are installed in fermentation tower are cross arrangement with pillar stiffener (3), one group of rotating shaft (4) layering horizontal anomalous movement is installed on the pillar stiffener (3), rotating shaft (4) is gone up the scarce shape liquid dish (6) of circle is installed, the place, circular arc summit that circle lacks shape liquid dish (6) connects elevating chain (5) by chain link (14), and the round breach that circle lacks shape liquid dish (6) is alternately reversed arrangement; Described circle lacks shape liquid dish (6) and is made up of the scarce shape chassis (7) of circle and cofferdam (8), cofferdam (8) is installed on the outer on the scarce shape chassis (7) of circle constitutes the scarce shape liquid dish (6) of circle; Wherein, it is lower than the height of circular arc cofferdam (16) that circle lacks the round breach cofferdam (12) of shape liquid dish (6), and the round breach cofferdam (12) of the scarce shape liquid dish (6) of circle lacks shape chassis (7) with circle and is 100-120 ° of inclination angle.
2. liquid dynamic surface fermentation tower according to claim 1 is characterized in that: top cover (2) is gone up the L shaped feed-pipe of installation (9) and is stretched in the tower to the scarce shape liquid dish of the first layer circle.
3. liquid dynamic surface fermentation tower according to claim 1 is characterized in that: at the discharge nozzle (11) of the bottom of tower body (1) mounting strap bleeder valve (10).
4. liquid dynamic surface fermentation tower according to claim 1 is characterized in that: the round indentation, there that lacks shape liquid dish (6) at circle is installed software drainage part (13) to the scarce shape liquid dish of lower floor circle.
5. liquid dynamic surface fermentation tower according to claim 1 is characterized in that: two support bars (15) and rotating shaft (4) formation triangular supports are installed in the bottom that lacks shape liquid dish (6) at circle, and wherein an end points is positioned at the center in breach cofferdam, garden (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101224413A CN101294126B (en) | 2008-05-28 | 2008-05-28 | Liquid dynamic surface fermentation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101224413A CN101294126B (en) | 2008-05-28 | 2008-05-28 | Liquid dynamic surface fermentation tower |
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| Publication Number | Publication Date |
|---|---|
| CN101294126A CN101294126A (en) | 2008-10-29 |
| CN101294126B true CN101294126B (en) | 2011-06-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008101224413A Expired - Fee Related CN101294126B (en) | 2008-05-28 | 2008-05-28 | Liquid dynamic surface fermentation tower |
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| Country | Link |
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| CN (1) | CN101294126B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102676376A (en) * | 2012-05-09 | 2012-09-19 | 顾立众 | Liquid stirring-free overlapped fermentation tower |
| CN103756887A (en) * | 2013-12-31 | 2014-04-30 | 江苏元洲生物工程有限公司 | Continuous flow fermentation tank |
| CN105062864B (en) * | 2015-08-04 | 2017-09-08 | 辽宁光华酿造有限公司 | Vinegar prepares fermentation tower |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100999708A (en) * | 2006-12-26 | 2007-07-18 | 沈阳农业大学 | Automotically feeding-discharging sealing type solid fermenting tank and fermentation process thereof |
| CN201072795Y (en) * | 2007-03-29 | 2008-06-11 | 董春国 | Batteries charger |
-
2008
- 2008-05-28 CN CN2008101224413A patent/CN101294126B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100999708A (en) * | 2006-12-26 | 2007-07-18 | 沈阳农业大学 | Automotically feeding-discharging sealing type solid fermenting tank and fermentation process thereof |
| CN201072795Y (en) * | 2007-03-29 | 2008-06-11 | 董春国 | Batteries charger |
Non-Patent Citations (1)
| Title |
|---|
| 李建华等.立式静态固态发酵罐的研制.<中国酿造>.2006,(第9期),49-52. * |
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| CN101294126A (en) | 2008-10-29 |
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Application publication date: 20081029 Assignee: Jiangsu Sumei Food Co., Ltd. Assignor: Gu Lizhong Contract record no.: 2012320000957 Denomination of invention: Liquid dynamic surface fermentation tower Granted publication date: 20110601 License type: Exclusive License Record date: 20120921 |
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