CN105130521A - Production technology for biological organic fertilizer special for tobacco - Google Patents
Production technology for biological organic fertilizer special for tobacco Download PDFInfo
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- CN105130521A CN105130521A CN201510370403.XA CN201510370403A CN105130521A CN 105130521 A CN105130521 A CN 105130521A CN 201510370403 A CN201510370403 A CN 201510370403A CN 105130521 A CN105130521 A CN 105130521A
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- tobacco leaf
- tobacco
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- organic fertilizer
- fertilizer special
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Abstract
The invention provides a production technology for a biological organic fertilizer special for tobacco. The technology comprises magnetic selection, crushing, pilling and fermentation, drying and shaping, adding auxiliary materials, drying and pelletizing, and packaging and storage. The production technology is simple, the material resource utilization rate is high, fertility is endurable, and pertinency is strong. Also, waste or deteriorated tobacco is once more effectively fully utilized, on the one hand, the cost of the fertilizer raw materials is reduced, and on the other hand, the pertinency of the fertilizer efficiency is improved, and thus growth demand of tobacco is relatively well satisfied.
Description
Technical field
The present invention relates to a kind of preparation technology of fertilizer, is exactly one to grow tobacco bio-organic fertilizer special production technique.
Background technology
At present in the planting process of tobacco leaf, in order to improve the growth quality of tobacco leaf, improve yield of tobacco, therefore often fertilising operation can be carried out to tobacco leaf as required when tobacco leaf planting, but when applying fertilizer, the presently used fertilizer fertilizer that versatility is stronger often, although can one meet tobacco leaf grow general needs, but effectively can not grow the trace element required for producing for tobacco leaf and carry out accurate proportioning, therefore significantly limit the performance of fertilizer efficiency, simultaneously, the raw material of current institute manure use also often comes from other organic materials and gets through preparations such as fermentations, therefore the cost of raw material is higher, to scrap for some simultaneously at present, the rotten tobacco leaf that waits also lacks corresponding recycling mode, therefore the utilization of materials that also result in tobacco leaf is not enough, to this present situation, in the urgent need to developing a kind of brand-new tobacco leaf planting fertilizer special for organic, with the needs that satisfied reality uses.
Summary of the invention
The object of this invention is to provide and the invention provides one and to grow tobacco bio-organic fertilizer special production technique.
In order to achieve the above object, the invention provides following technical scheme:
One grows tobacco bio-organic fertilizer special production technique, comprises the steps:
The first step, magnetic separation, utilizes electromagnetic separation equipment, carries out magnetic separation process to tobacco leaf, and is recycled by metallic substance in tobacco leaf etc.;
Second step, pulverizes, utilizes pulverizer to pulverize on the tobacco leaf operated through magnetic separation, obtain the strip tobacco leaf particle that length is 5-30 millimeters after pulverizing;
3rd step, windrow ferments, tobacco leaf particle after pulverizing is piled up, and particle heap minimum diameter is not less than 100 centimetres, is highly not less than 50 centimetres, then in particle heap, evenly biological fermentation bacterium, excrement of animals and water is sprayed, then with plastic film, particle heap is carried out coated, and keep leavening temperature to be 25 DEG C-60 DEG C, and fermentation time is not less than 7 days, separately every at least 2 days, particle heap is once stirred, the fermented liquid produced is collected simultaneously in fermenting process;
4th step, dry forming, be loaded in forming mould by the tobacco leaf particle after processing by fermentation, then utilize high temperature to carry out drying, dried tobacco leaf particle water content is not more than 20%;
5th step, pulverizes shaping, through saying that the tobacco leaf particle of super-dry process utilizes pulverizer to pulverize, and is prepared into the little material particles with 2 millimeters of diameter;
6th step, add auxiliary material, the fermented liquid collected in 3rd step is added in the liquid of natural pond, and in the liquid of natural pond, add starch, wheat bran, xanthohumic acid, zinc oxide, potassium oxide, urea and flyash simultaneously, and be prepared into solution, then material particles to be added in solution and to stir, and separately keeping 20 DEG C of-50 DEG C of constant temperature at the uniform velocity to stir in the same way when stirring, and churning time is 10-50 minutes;
7th step, drying-granulating, carries out drying treatment by the mixture through stir process in the 5th step, and drying treatment is simultaneously, and separately carry out granulation operation, be 1-5 millimeters through the compound particles diameter prepared by granulation operation, water content is not more than 5%;
8th step, packaging stores, and utilizes vacuum seal device to carry out packing and depositing after the particle of granulation processing preparation is cooled to normal temperature.
Further, the combination that the tobacco leaf in the described the first step is fresh tobacco leaves, rot in a kind of or Arbitrary Sets of tobacco leaf or dry tobacco leaf.
Further, when described second step ferments, wherein excrement of animals total amount is not more than 20% of tobacco leaf particle total amount;
Further, in the 6th described step by mass percentage, wherein fermented liquid 10%-20%, starch 3%-6%, wheat bran 3%-6%, xanthohumic acid 0.5%-2%, zinc oxide 5%-15%, potassium oxide 5%-15%, urea 5%-15%, flyash 30%-60%, material particles 40%-80%, natural pond liquid 10%-30%.
Production technique of the present invention is simple, material resource utilization ratio is high, and fertility is lasting, with strong points, separately can effectively again make full use of discarded or rotten tobacco leaf simultaneously, on the one hand reduce the raw-material cost of fertilizer, also improve the specific aim of fertilizer efficiency on the other hand, thus better meet the needs that tobacco leaf grows.
Accompanying drawing explanation
In order to be illustrated more clearly in the embodiment of the present invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is present invention process schema.
Embodiment
Be clearly and completely described technical scheme of the present invention below in conjunction with accompanying drawing of the present invention, obviously, described embodiment is only the present invention's part embodiment, instead of whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of protection of the invention.
Embodiment 1
As shown in Figure 1 one grows tobacco bio-organic fertilizer special production technique, comprises the steps:
The first step, magnetic separation, utilizes electromagnetic separation equipment, carries out magnetic separation process to tobacco leaf, and is recycled by metallic substance in tobacco leaf etc.;
Second step, pulverizes, utilizes pulverizer to pulverize on the tobacco leaf operated through magnetic separation, obtain the strip tobacco leaf particle that length is 15 millimeters after pulverizing;
3rd step, windrow ferments, tobacco leaf particle after pulverizing is piled up, and particle heap diameter is 100 centimetres, be highly 50 centimetres, then in particle heap, evenly biological fermentation bacterium, excrement of animals and water is sprayed, wherein excrement of animals total amount is 15% of tobacco leaf particle total amount, then with plastic film, particle heap is carried out coated, and keep leavening temperature to be 30 DEG C, and fermentation time is not less than 10 days, separately every 2 days, particle heap is once stirred, the fermented liquid produced is collected simultaneously in fermenting process;
4th step, dry forming, be loaded in forming mould by the tobacco leaf particle after processing by fermentation, then utilize high temperature to carry out drying, dried tobacco leaf particle is moisture is 15%;
5th step, pulverizes shaping, through saying that the tobacco leaf particle of super-dry process utilizes pulverizer to pulverize, and is prepared into the material particles that diameter is 5 millimeters;
6th step, add auxiliary material, the fermented liquid collected in 3rd step is added in the liquid of natural pond, and in the liquid of natural pond, add starch simultaneously, wheat bran, xanthohumic acid, zinc oxide, potassium oxide, urea and flyash, and be prepared into solution, wherein press massfraction, fermented liquid 10, starch 3%, wheat bran 6%, xanthohumic acid 0.5%, zinc oxide 5%, potassium oxide 10%, urea 10%, flyash 50%, material particles 60%, surplus is natural pond liquid, then material particles to be added in solution and to stir, and separately keep 30 DEG C of constant temperature at the uniform velocity to stir in the same way when stirring, and churning time is 30 minutes,
7th step, drying-granulating, carries out drying treatment by the mixture through stir process in the 5th step, and drying treatment is simultaneously, and separately carrying out granulation operation, is 3 millimeters through the compound particles diameter prepared by granulation operation, and water content is 3%;
8th step, packaging stores, and utilizes vacuum seal device to carry out packing and depositing after the particle of granulation processing preparation is cooled to normal temperature.
Embodiment 2
The first step, magnetic separation, utilizes electromagnetic separation equipment, carries out magnetic separation process to tobacco leaf, and is recycled by metallic substance in tobacco leaf etc.;
Second step, pulverizes, utilizes pulverizer to pulverize on the tobacco leaf operated through magnetic separation, obtain the strip tobacco leaf particle that length is 10 millimeters after pulverizing;
3rd step, windrow ferments, tobacco leaf particle after pulverizing is piled up, and particle heap diameter is 200 centimetres, be highly 100 centimetres, then in particle heap, evenly biological fermentation bacterium, excrement of animals and water is sprayed, wherein excrement of animals total amount is 10% of tobacco leaf particle total amount, then with plastic film, particle heap is carried out coated, and keep leavening temperature to be 40 DEG C, and fermentation time is 9 days, separately every 2 days, particle heap is once stirred, the fermented liquid produced is collected simultaneously in fermenting process;
4th step, dry forming, be loaded in forming mould by the tobacco leaf particle after processing by fermentation, then utilize high temperature to carry out drying, dried tobacco leaf particle is moisture is 15%;
5th step, pulverizes shaping, through saying that the tobacco leaf particle of super-dry process utilizes pulverizer to pulverize, and is prepared into the material particles that diameter is 5 millimeters;
6th step, add auxiliary material, the fermented liquid collected in 3rd step is added in the liquid of natural pond, and in the liquid of natural pond, add starch simultaneously, wheat bran, xanthohumic acid, zinc oxide, potassium oxide, urea and flyash, and be prepared into solution, wherein press massfraction, fermented liquid 11, starch 5%, wheat bran 4%, xanthohumic acid 1%, zinc oxide 10%, potassium oxide 10%, urea 10%, flyash 40%, material particles 60%, surplus is natural pond liquid %, then material particles to be added in solution and to stir, and separately keep 35 DEG C of constant temperature at the uniform velocity to stir in the same way when stirring, and churning time is 40 minutes,
7th step, drying-granulating, carries out drying treatment by the mixture through stir process in the 5th step, and drying treatment is simultaneously, and separately carrying out granulation operation, is 5 millimeters through the compound particles diameter prepared by granulation operation, and water content is 1%;
8th step, packaging stores, and utilizes vacuum seal device to carry out packing and depositing after the particle of granulation processing preparation is cooled to normal temperature.
Production technique of the present invention is simple, material resource utilization ratio is high, and fertility is lasting, with strong points, separately can effectively again make full use of discarded or rotten tobacco leaf simultaneously, on the one hand reduce the raw-material cost of fertilizer, also improve the specific aim of fertilizer efficiency on the other hand, thus better meet the needs that tobacco leaf grows.
The above; be only the specific embodiment of the present invention, but protection scope of the present invention is not limited thereto, is anyly familiar with those skilled in the art in the technical scope that the present invention discloses; change can be expected easily or replace, all should be encompassed within protection scope of the present invention.Therefore, protection scope of the present invention should described be as the criterion with the protection domain of claim.
Claims (4)
1. one to grow tobacco bio-organic fertilizer special production technique, it is characterized in that: described tobacco bio-organic fertilizer special production technique comprises the steps:
The first step, magnetic separation, utilizes electromagnetic separation equipment, carries out magnetic separation process to tobacco leaf, and is recycled by metallic substance in tobacco leaf etc.;
Second step, pulverizes, utilizes pulverizer to pulverize on the tobacco leaf operated through magnetic separation, obtain the strip tobacco leaf particle that length is 5-30 millimeters after pulverizing;
3rd step, windrow ferments, tobacco leaf particle after pulverizing is piled up, and particle heap minimum diameter is not less than 100 centimetres, is highly not less than 50 centimetres, then in particle heap, evenly biological fermentation bacterium, excrement of animals and water is sprayed, then with plastic film, particle heap is carried out coated, and keep leavening temperature to be 25 DEG C-60 DEG C, and fermentation time is not less than 7 days, separately every at least 2 days, particle heap is once stirred, the fermented liquid produced is collected simultaneously in fermenting process;
4th step, dry forming, be loaded in forming mould by the tobacco leaf particle after processing by fermentation, then utilize high temperature to carry out drying, dried tobacco leaf particle water content is not more than 20%;
5th step, pulverizes shaping, through saying that the tobacco leaf particle of super-dry process utilizes pulverizer to pulverize, and is prepared into the little material particles with 2 millimeters of diameter;
6th step, add auxiliary material, the fermented liquid collected in 3rd step is added in the liquid of natural pond, and in the liquid of natural pond, add starch, wheat bran, xanthohumic acid, zinc oxide, potassium oxide, urea and flyash simultaneously, and be prepared into solution, then material particles to be added in solution and to stir, and separately keeping 20 DEG C of-50 DEG C of constant temperature at the uniform velocity to stir in the same way when stirring, and churning time is 10-50 minutes;
7th step, drying-granulating, carries out drying treatment by the mixture through stir process in the 5th step, and drying treatment is simultaneously, and separately carry out granulation operation, be 1-5 millimeters through the compound particles diameter prepared by granulation operation, water content is not more than 5%;
8th step, packaging stores, and utilizes vacuum seal device to carry out packing and depositing after the particle of granulation processing preparation is cooled to normal temperature.
2. according to claim 1 one to grow tobacco bio-organic fertilizer special production technique, it is characterized in that: the tobacco leaf in the described the first step is fresh tobacco leaves, the combination of rotting in a kind of or Arbitrary Sets of tobacco leaf or dry tobacco leaf.
3. according to claim 1 one to grow tobacco bio-organic fertilizer special production technique, it is characterized in that: when described second step ferments, wherein excrement of animals total amount is not more than 20% of tobacco leaf particle total amount.
4. according to claim 1 one to grow tobacco bio-organic fertilizer special production technique, it is characterized in that: in the 6th described step by mass percentage, wherein fermented liquid 10%-20%, starch 3%-6%, wheat bran 3%-6%, xanthohumic acid 0.5%-2%, zinc oxide 5%-15%, potassium oxide 5%-15%, urea 5%-15%, flyash 30%-60%, material particles 40%-80%, natural pond liquid 10%-30%.
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| CN201510370403.XA CN105130521A (en) | 2015-06-30 | 2015-06-30 | Production technology for biological organic fertilizer special for tobacco |
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| CN201510370403.XA CN105130521A (en) | 2015-06-30 | 2015-06-30 | Production technology for biological organic fertilizer special for tobacco |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102887742A (en) * | 2012-11-05 | 2013-01-23 | 师宗海利食品有限责任公司 | Process for producing bioorganic fertilizer by utilizing fresh tobacco leaf |
| CN102887754A (en) * | 2012-11-05 | 2013-01-23 | 师宗海利食品有限责任公司 | Process for producing marsh gas and bioorganic fertilizer by utilizing tobacco waste |
| CN103387426A (en) * | 2013-07-31 | 2013-11-13 | 常熟市常福有机复合肥有限公司 | Tobacco biological organic fertilizer |
| CN103708860A (en) * | 2013-12-27 | 2014-04-09 | 贵州凤泰禽业有限公司 | Organic fertilizer prepared from chicken manure and tobacco and preparation method thereof |
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2015
- 2015-06-30 CN CN201510370403.XA patent/CN105130521A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102887742A (en) * | 2012-11-05 | 2013-01-23 | 师宗海利食品有限责任公司 | Process for producing bioorganic fertilizer by utilizing fresh tobacco leaf |
| CN102887754A (en) * | 2012-11-05 | 2013-01-23 | 师宗海利食品有限责任公司 | Process for producing marsh gas and bioorganic fertilizer by utilizing tobacco waste |
| CN103387426A (en) * | 2013-07-31 | 2013-11-13 | 常熟市常福有机复合肥有限公司 | Tobacco biological organic fertilizer |
| CN103708860A (en) * | 2013-12-27 | 2014-04-09 | 贵州凤泰禽业有限公司 | Organic fertilizer prepared from chicken manure and tobacco and preparation method thereof |
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Application publication date: 20151209 |