CN103980013B - A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control - Google Patents
A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control Download PDFInfo
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- CN103980013B CN103980013B CN201410230923.6A CN201410230923A CN103980013B CN 103980013 B CN103980013 B CN 103980013B CN 201410230923 A CN201410230923 A CN 201410230923A CN 103980013 B CN103980013 B CN 103980013B
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Abstract
A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control, comprise first, second fermentation cylinder horizontal be arranged side by side, by the first and second Matter Transfer channel connections between fermentation cylinder, first fermentation top, cylinder one end is provided with feeding mouth, sets out feed bin door in the second Matter Transfer channel bottom; Tubular shaft is equipped with in each fermentation cylinder inside, two ends are provided with end cap, one end of tubular shaft is connected with the output shaft of servomotor, the other end of tubular shaft is connected with air volume adjustable gas blower through temp and humidity regulator, tubular shaft is welded with helical mixing blade, baffle plate is welded with at the end of helical mixing blade, tubular shaft is provided with ventilating pit, the present invention adopts humiture control and circulation stirring, not only accelerate fermenting speed, and improve fermented quality, make material fermentation more full and uniform.
Description
Technical field
The present invention relates to organic fertilizer production processing unit technical field, particularly relate to a kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control.
Background technology
Along with the fast development of Chinese society economy and urbanization, the ecological agriculture is more and more extremely paid attention to, and green food is also more and more subject to the favor of people.Out, the demand of fertilizer increases the drawback exposed day by day of excessive use chemical fertilizer day by day, and the development of fertilizer industry is become better and better.But the production unit of fertilizer backwardness relatively, lacks specific equipment.Current great majority equipment be all from mineral manure production unit transformation, production efficiency is lower.The main organic fertilizer fermentation mode used mainly contains now: the fermentation of bar buttress formula, trough type fermentation and tower fermentation.Although the formula fermentation of bar buttress and trough type fermentation technique are comparatively simply, all there is floor space large, need to build factory building, the problems such as the production cycle is long; Fermentation tower floor space is relatively minimum, and efficiency is relatively high, but fermentation time at least one week, and cost of equipment and equipment maintenance cost high.
Summary of the invention
In order to overcome the shortcoming of above-mentioned prior art, the object of the present invention is to provide a kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control, there is the advantage that structure is simple, floor space is little, energy-efficient, fermentation period is short.
In order to achieve the above object, the technical scheme that the present invention takes is:
A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control, comprise horizontal first fermentation cylinder 3 and the second fermentation cylinder 4 be arranged side by side, be communicated with the second Matter Transfer passage 15 by the first Matter Transfer passage 14 between first fermentation cylinder 3 and the second fermentation cylinder 4, first fermentation top, cylinder 3 one end is provided with feeding mouth 16, bottom the second Matter Transfer passage 15, set out feed bin door 17;
Tubular shaft 11 is equipped with in each fermentation cylinder inside, two ends are provided with end cap 18, one end of tubular shaft 11 is connected with the output shaft of servomotor 6 by the first tubular shaft joint 10, shaft coupling 9, speed reduction unit 7 successively, the other end of tubular shaft 11 is connected with air volume adjustable gas blower 1 by the second tubular shaft joint 21, temp and humidity regulator 2 successively, tubular shaft 11 is welded with helical mixing blade 12, be welded with baffle plate 13 at the end of helical mixing blade 12, tubular shaft 11 is provided with ventilating pit 22.
The end cap 18 at described first fermentation cylinder 3 and the second fermentation cylinder 4 two ends is connected on the first support 8 and the second support 19, the first support 8 and between the second support 19 and ground, cushion blocking 20 is housed.
The first described fermentation cylinder 3 and the second fermentation cylinder 4 all have inside and outside two-layer barrel, are provided with thermal insulation layer 5 in the middle of inside and outside two-layer barrel.
Thermal insulation layer is provided with in the first described Matter Transfer passage 14 and the second Matter Transfer passage 15.
Effect of the present invention: because the present invention adopts humiture control system, can not only provide sufficient oxygen to fermentation materials, and fermentation humiture can be made to remain in the most active scope of aerobic bacteria always; Circulation stirring makes material be uniformly mixed in two fermentation cylinders in addition, and circulating fermentation, so not only accelerates fermenting speed, and improves fermented quality, makes material fermentation more full and uniform.
Accompanying drawing explanation
Fig. 1 is vertical view of the present invention.
Fig. 2 is the axis horizontal cross of Fig. 1 along tubular shaft 11.
Embodiment
Below in conjunction with accompanying drawing, the present invention is described in detail.
See figures.1.and.2, a kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control, comprise horizontal first fermentation cylinder 3 and the second fermentation cylinder 4 be arranged side by side, be communicated with the second Matter Transfer passage 15 by the first Matter Transfer passage 14 between first fermentation cylinder 3 and the second fermentation cylinder 4, first fermentation top, cylinder 3 one end is provided with feeding mouth 16, feed bin door 17 is set out bottom the second Matter Transfer passage 15, when discharging door 17 is opened, can discharging;
Tubular shaft 11 is equipped with in each fermentation cylinder inside, two ends are provided with end cap 18, one end of tubular shaft 11 is successively by the first tubular shaft joint 10, shaft coupling 9, speed reduction unit 7 is connected with the output shaft of servomotor 6, the other end of tubular shaft 11 is successively by the second tubular shaft joint 21, temp and humidity regulator 2 is connected with air volume adjustable gas blower 1, tubular shaft 11 is welded with helical mixing blade 12, helical mixing blade 12 can realize being uniformly mixed material limit, while the effect of pushing ahead, baffle plate 13 is welded with at the end of helical mixing blade 12, material in fermentation cylinder can be advanced the first Matter Transfer passage 14 and the second Matter Transfer passage 15 by baffle plate 13, material is entered in another fermentation cylinder and continues fermentation, tubular shaft 11 is provided with ventilating pit 22, air enters in the first fermentation cylinder 3 and the second fermentation cylinder 4 from ventilating pit 22, heating and moistening is carried out to fermentation cylinder, make temperature in cylinder, humidity remains in the most active scope of aerobic bacteria.
The end cap 18 at described first fermentation cylinder 3 and the second fermentation cylinder 4 two ends is connected on the first support 8 and the second support 19, the first support 8 and between the second support 19 and ground, cushion blocking 20 is housed.
The first described fermentation cylinder 3 and the second fermentation cylinder 4 all have inside and outside two-layer barrel, are provided with thermal insulation layer 5 in the middle of inside and outside two-layer barrel.
Thermal insulation layer is provided with in the first described Matter Transfer passage 14 and the second Matter Transfer passage 15.
Principle of work of the present invention is:
The yeasting of this equipment mainly in order to provide optimum to solid organic fertilizer aerobic fermentation, and then raise the efficiency and fermented quality, shorten fermentation time.The material mixed adds from feeding mouth 16, simultaneously, agitation cycle and humiture control work, servomotor 6 drives tubular shaft 11 to rotate, agitation cycle is carried out by helical mixing blade 12, baffle plate 13, the material stirring at feeding mouth 16 place is also sent to forward, makes material be full of the first fermentation cylinder 3 and the second fermentation cylinder 4, the ventilating pit 22 that temp and humidity regulator 2 is provided with by air volume adjustable gas blower 1 and tubular shaft 11 carries out humiture control in the first fermentation cylinder 3 and the second fermentation cylinder 4, air volume adjustable gas blower 1 will be adjusted to design temperature through temp and humidity regulator 2, the fresh air of humidity is sent in the first fermentation cylinder 3 and the second fermentation cylinder 4, warming and humidifying is carried out to the material just added, air after warming and humidifying, not only be fed into the oxygen needed for aerobic fermentation, and ensure that temperature needed for fermentation, humidity, being unlikely to blows on material dries up, after reinforced, feeding mouth 16 is closed, be incubated, moisturizing is fermented, according to fermentation situation, when fermentation requisite oxygen QI-insufficiency or humidity are not suitable for, again start servomotor 6, temp and humidity regulator 2 and air volume adjustable gas blower 1, material is made to carry out circulation stirring in the first fermentation cylinder 3 and the second fermentation cylinder 4, the air after humiture control device 2 warming and humidifying sent into by air volume adjustable gas blower 1, ozone is fully contacted with material, for aerobic fermentation provides sufficient oxygen and moisture, make system temperature, humidity remains in the most active scope of aerobic bacteria, after fermentation completes, discharging door 17 is opened, start servomotor 6, the material fermented is exported in fermentation cylinder.
Claims (4)
1. the spiral forced cyclic type bitubular organic fertilizer fermentation equipment of an AC Servo Control, comprise horizontal first fermentation cylinder (3) and the second fermentation cylinder (4) that are arranged side by side, it is characterized in that: be communicated with the second Matter Transfer passage (15) by the first Matter Transfer passage (14) between the first fermentation cylinder (3) and the second fermentation cylinder (4), first fermentation cylinder (3) top, one end is provided with feeding mouth (16), sets out feed bin door (17) in the second Matter Transfer passage (15) bottom;
Tubular shaft (11) is equipped with in each fermentation cylinder inside, two ends are provided with end cap (18), one end of tubular shaft (11) is successively by the first tubular shaft joint (10), shaft coupling (9), speed reduction unit (7) is connected with the output shaft of servomotor (6), the other end of tubular shaft (11) is successively by the second tubular shaft joint (21), temp and humidity regulator (2) is connected with air volume adjustable gas blower (1), tubular shaft (11) is welded with helical mixing blade (12), baffle plate (13) is welded with at the end of helical mixing blade (12), tubular shaft (11) is provided with ventilating pit (22).
2. the spiral forced cyclic type bitubular organic fertilizer fermentation equipment of a kind of AC Servo Control according to claim 1, it is characterized in that: described first fermentation cylinder (3) and the second end cap (18) fermenting cylinder (4) two ends are connected on the first support (8) and the second support (19), the first support (8) and between the second support (19) and ground, cushion blocking (20) is housed.
3. the spiral forced cyclic type bitubular organic fertilizer fermentation equipment of a kind of AC Servo Control according to claim 1, it is characterized in that: the first described fermentation cylinder (3) and the second fermentation cylinder (4) all have inside and outside two-layer barrel, are provided with thermal insulation layer (5) in the middle of inside and outside two-layer barrel.
4. the spiral forced cyclic type bitubular organic fertilizer fermentation equipment of a kind of AC Servo Control according to claim 1, is characterized in that: be provided with thermal insulation layer in the first described Matter Transfer passage (14) and the second Matter Transfer passage (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410230923.6A CN103980013B (en) | 2014-05-28 | 2014-05-28 | A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410230923.6A CN103980013B (en) | 2014-05-28 | 2014-05-28 | A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control |
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| Publication Number | Publication Date |
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| CN103980013A CN103980013A (en) | 2014-08-13 |
| CN103980013B true CN103980013B (en) | 2015-10-21 |
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| CN201410230923.6A Expired - Fee Related CN103980013B (en) | 2014-05-28 | 2014-05-28 | A kind of spiral forced cyclic type bitubular organic fertilizer fermentation equipment of AC Servo Control |
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Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106431542A (en) * | 2016-09-18 | 2017-02-22 | 朱超英 | Stirring fermentation machine, system and method |
| CN106747750A (en) * | 2016-12-30 | 2017-05-31 | 重庆市益丰生物肥有限公司 | Organic fertilizer circulating fermentation device |
| CN107376694A (en) * | 2017-08-29 | 2017-11-24 | 吴江市金鑫塑料厂 | A kind of layer-stepping agitating device |
| CN109704832B (en) * | 2019-01-29 | 2021-10-29 | 山东大学 | Horizontal barrel type quick fermentation device for biological bacterial manure |
| CN114349559A (en) * | 2021-12-23 | 2022-04-15 | 长沙中联重科环境产业有限公司 | Mixing and stirring device for aerobic fermentation tank and aerobic fermentation system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2864672A (en) * | 1953-12-28 | 1958-12-16 | Edward H Brooks Jr | Organic waste reduction apparatus |
| CN102441941A (en) * | 2011-11-09 | 2012-05-09 | 冯忠绪 | Single horizontal shaft vibration mixer |
| CN102674921A (en) * | 2012-06-15 | 2012-09-19 | 广州农冠生物科技有限公司 | Stationary type organic material fermentation machine and fermentation technology thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3907879A1 (en) * | 1989-03-10 | 1990-09-13 | Sohm Ohg Techn Einrichtung Fue | METHOD AND DEVICE FOR COMPOSITION PROCESSING FOR MUSHROOM BREEDING |
| KR100867782B1 (en) * | 2007-01-12 | 2008-11-10 | 김봉섭 | Rotary mixing dryer |
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2014
- 2014-05-28 CN CN201410230923.6A patent/CN103980013B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2864672A (en) * | 1953-12-28 | 1958-12-16 | Edward H Brooks Jr | Organic waste reduction apparatus |
| CN102441941A (en) * | 2011-11-09 | 2012-05-09 | 冯忠绪 | Single horizontal shaft vibration mixer |
| CN102674921A (en) * | 2012-06-15 | 2012-09-19 | 广州农冠生物科技有限公司 | Stationary type organic material fermentation machine and fermentation technology thereof |
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| CN103980013A (en) | 2014-08-13 |
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Granted publication date: 20151021 Termination date: 20180528 |