CN108243900A - A kind of bulb of thunberg fritillary plantation substrate, preparation process and system - Google Patents
A kind of bulb of thunberg fritillary plantation substrate, preparation process and system Download PDFInfo
- Publication number
- CN108243900A CN108243900A CN201810100209.3A CN201810100209A CN108243900A CN 108243900 A CN108243900 A CN 108243900A CN 201810100209 A CN201810100209 A CN 201810100209A CN 108243900 A CN108243900 A CN 108243900A
- Authority
- CN
- China
- Prior art keywords
- bamboo
- bulb
- bamboo charcoal
- bamboo vinegar
- retort
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000002360 preparation method Methods 0.000 title claims abstract description 63
- 241000935235 Fritillaria meleagris Species 0.000 title claims abstract description 58
- 239000000758 substrate Substances 0.000 title claims abstract description 33
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims abstract description 233
- 235000017491 Bambusa tulda Nutrition 0.000 claims abstract description 233
- 241001330002 Bambuseae Species 0.000 claims abstract description 233
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims abstract description 233
- 239000011425 bamboo Substances 0.000 claims abstract description 233
- 235000021419 vinegar Nutrition 0.000 claims abstract description 122
- 239000000052 vinegar Substances 0.000 claims abstract description 122
- 239000003610 charcoal Substances 0.000 claims abstract description 115
- 239000011159 matrix material Substances 0.000 claims abstract description 34
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 150000001875 compounds Chemical class 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 92
- 239000000843 powder Substances 0.000 claims description 66
- 241000196324 Embryophyta Species 0.000 claims description 45
- 239000000463 material Substances 0.000 claims description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 239000004927 clay Substances 0.000 claims description 25
- 239000000428 dust Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 23
- 239000012530 fluid Substances 0.000 claims description 21
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 20
- 239000011707 mineral Substances 0.000 claims description 20
- 238000009833 condensation Methods 0.000 claims description 19
- 230000005494 condensation Effects 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 10
- 210000003608 fece Anatomy 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 8
- 229910052700 potassium Inorganic materials 0.000 claims description 8
- 239000000779 smoke Substances 0.000 claims description 8
- 235000019738 Limestone Nutrition 0.000 claims description 7
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 7
- 239000006028 limestone Substances 0.000 claims description 7
- 239000011591 potassium Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 7
- 238000010792 warming Methods 0.000 claims description 7
- 238000004821 distillation Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims 1
- 238000010025 steaming Methods 0.000 claims 1
- 235000015097 nutrients Nutrition 0.000 abstract description 9
- 239000003337 fertilizer Substances 0.000 abstract description 4
- 238000009395 breeding Methods 0.000 abstract description 3
- 230000001488 breeding effect Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 19
- 230000000052 comparative effect Effects 0.000 description 10
- 241000894006 Bacteria Species 0.000 description 8
- 238000004886 process control Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000017525 heat dissipation Effects 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 238000013329 compounding Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 238000001256 steam distillation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- -1 ammonium ions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000002391 heterocyclic compounds Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000009331 sowing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C5/00—Production of pyroligneous acid distillation of wood, dry distillation of organic waste
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Pest Control & Pesticides (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Cultivation Of Plants (AREA)
- Carbon And Carbon Compounds (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses a kind of bulb of thunberg fritillary plantation substrate, preparation process and systems, it compounds to obtain a kind of bulb of thunberg fritillary plantation substrate using bamboo charcoal and refined bamboo vinegar as primary raw material, not only the nursery of bulb had been used directly for, but also can directly apply plot conduct and accompany fertilizer ground substance.The maximization that nutrient needed for the breeding of bulb of thunberg fritillary bulb is realized using the cultivation matrix is compounded, and is ensured maximally utilizing for critical nutrients, is finally realized the raising of bulb of thunberg fritillary vegetative propagation emergence rate.
Description
Technical field
The present invention relates to a kind of cultivation matrixes, and in particular to a kind of bulb of thunberg fritillary plantation substrate, preparation system and technique.Belong to
In bulb of thunberg fritillary technical field of cultivation.
Background technology
The solution efficiently emerged for bulb of thunberg fritillary is not found at present, is all traditional nursery means, from agrotechnical angle
Degree goes to improve planting percent.Bulb of thunberg fritillary is usually to form bulb in summer, and more after the summer, nursery will be used as in 10 annual~November
The bulb on basis digs up to rearrange again and is seeded into ground namely forms bulb to sowing (intermediate meeting next time in bulb of thunberg fritillary
The high bulb of a collection of commodity is dug out to be peddled) during, the bulb as seedling substrate will be embedded in ground borough chief up to 2~3
As long as month, encounter the time more than rainwater, bulb it is rotten be it is very serious, directly result in the reduction of the yield of bulb of thunberg fritillary, bring through
Loss in Ji.
Bulb of thunberg fritillary mainly realizes that expansion is numerous by bulb breeding and tissue cultures in process of production.It is low for bulb of thunberg fritillary emergence rate
The problem of, it is related to the nursery of bulb of thunberg fritillary, is badly in need of a kind of seedling medium at present, according to the nutrient demand in bulb of thunberg fritillary bulb plumule emergence
Promote bulb seedling to formulate efficient formula.
Invention content
The purpose of the present invention is to overcome above-mentioned the deficiencies in the prior art, provide a kind of bulb of thunberg fritillary plantation substrate, prepare
Technique and system.
To achieve the above object, the present invention uses following technical proposals：
A kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort, connect the gas outlet of retort with
Condensing plant opens condensing plant, closes bamboo charcoal discharge port and activated carbon discharge nozzle, and material is heated with the heating rate of 0.1 DEG C/s
Temperature is to 250~350 DEG C, charing process 15~20 minutes in this temperature range, and the condensed equipment of bamboo vinegar steam stream of generation is cold
It coagulates for crude bamboo vinegar, and the bottom for passing through condensing plant is expelled to distilling apparatus；
(2) continue to heat material temperature to 300~350 DEG C, open bamboo charcoal discharge port, the bamboo charcoal of discharge is collected using tray,
And the cooling that tiles；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray, until residual in retort
1/20 that quality is input amount is stayed, closes bamboo charcoal discharge port；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon in retort, connects activated carbon
Discharge nozzle makes activated carbon slowly enter the distilling apparatus for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes condensation
Equipment exports, and avoids flowing back；
(5) distilling apparatus is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, generation
Enter refined bamboo vinegar reception device after the condensed conduit condensation of steam, stand 24 hours, filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
Preferably, in step (1), pressure reducing valve is opened slightly, for adjusting pressure in retort；In step (3), bamboo is closed
Pressure reducing valve is also turn off while charcoal discharge port.
Preferably, in step (1), the bamboo vinegar steam of generation is followed by two condensers, respectively from two condensers
The crude bamboo vinegar that condensation obtains is expelled to distilling apparatus by bottom.
Preferably, in step (4), in distilling apparatus, the mass ratio of activated carbon and crude bamboo vinegar is 1：12.
Preferably, in step (5), pH=3.4~4.8 of refined bamboo vinegar.
Preferably, the specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2~3 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 3~5 hours, cross 40 mesh sieve, obtain
Scorched clay dust powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5~5.8, stop sprinkling bamboo vinegar to get.
It is further preferred that in step (6-2), thickness of earth covering is 1cm on hay.
It is further preferred that in step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：
8。
It is further preferred that the whole-process control moisture in the preparation process of cultivation matrix, the water of final gained cultivation matrix
Weight content is divided to be less than 15%.
It is further preferred that step (6-4) is also granulated after stopping spraying bamboo vinegar, controls the appearance of cultivation matrix
Weight ranging from 1.15~1.27g/cm3。
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
Bulb of thunberg fritillary bulb nursery is carried out using above-mentioned cultivation matrix, specific method is：In late October, bulb of thunberg fritillary bulb is embedded in
In the cultivation matrix, institute's buried depth degree is 2 times, about 5~7cm of bulb of thunberg fritillary bulb diameter, and seedling raise period is 14~20 days.
The corresponding a kind of preparation system of bulb of thunberg fritillary plantation substrate of above-mentioned preparation process, including bamboo charcoal preparation facilities and bamboo
Vinegar liquid preparation facilities two parts, the bamboo charcoal preparation facilities are retort, and the main body of bamboo vinegar preparation facilities is condensing plant, charcoal
Change and be respectively equipped with gas outlet and bamboo charcoal discharge port at the top and bottom of stove, the lower section setting tray of bamboo charcoal discharge port, it is described go out
Gas port is connected to the top of condensing plant, and the bottom of condensing plant is connected with distilling apparatus；The bottom of the retort is additionally provided with
Activated carbon discharge nozzle, activated carbon discharge nozzle are connected to distilling apparatus；The distilling apparatus passes through condensation pipe and refined bamboo vinegar
Reception device connects.
Preferably, the bottom of the retort is additionally provided with pressure reducing valve, and the bamboo vinegar steam that being arranged on bottom can prevent leads to
Pressure reducing valve is crossed to lose.
Preferably, the condensing plant includes the first condenser and the second condenser of series connection, and the gas outlet of retort connects
It is connected to the top of the first condenser, the bottom of the first condenser is equipped with leakage fluid dram I and exhaust outlet, exhaust outlet and the second condenser
Top connects, and the bottom of the second condenser is equipped with leakage fluid dram II, and the leakage fluid dram I and leakage fluid dram II are respectively connected to distillation dress
It puts.
It is further preferred that the outside of first condenser and the second condenser be respectively arranged the first condensing water conduit and
Second condensing water conduit, condensed water enter from the bottom of the second condensing water conduit, and top outflow then flows into the first condensate pipe
The bottom in road is finally flowed out via the top of the first condensing water conduit.
Preferably, the material of the tray is stainless steel, is conducive to collected bamboo charcoal tiling heat dissipation.
Preferably, stirring rod is equipped in the distilling apparatus.
Beneficial effects of the present invention：
The present invention compounds to obtain a kind of bulb of thunberg fritillary plantation substrate using bamboo charcoal and refined bamboo vinegar as primary raw material, both can be with
The nursery of bulb is directly used in, while can directly apply plot conduct again and accompany fertilizer ground substance.Zhejiang is realized using the cultivation matrix
The maximization compounding of nutrient needed for the breeding of shellfish bulb, ensures maximally utilizing for critical nutrients, it is asexual numerous finally to realize bulb of thunberg fritillary
Grow the raising of emergence rate.The key problem in technology of the present invention is that the quality of bamboo charcoal and refined bamboo vinegar improves, and corresponding is to prepare work
The innovation of skill, it is specific as follows：
1st, bulb of thunberg fritillary growth is more sensitive for elements such as N, K, Mg, Zn, Cu, therefore in the process of cultivation matrix raw material compounding
It is middle to need to add in the more raw material of available nutrient, the high mountain mao bamboon of special ratios is formed with cow dung by specific calcine technology
The maximized bamboo charcoal of nutrient is imitated, makes it have physically better absorption property, fertilizer conservation effect is good, and the nutrient of compounding is avoided quickly to flow
It loses, slow release nutrient is more advantageous to bulb of thunberg fritillary bulb seedling.Wherein, the addition of cow dung helps to improve the ash content of gained bamboo charcoal,
Increase effective nitrogen content.
2nd, the difference of bamboo vinegar refines mode and is affected for the property of itself, needs to control the refined bamboo vinegar of gained
PH=3.4~4.8 of liquid are proper, organic matter mass content 8% or so (organic acid, phenols, ketone, aldehydes, alcohols, three
Terpene, heterocyclic compound), the bamboo vinegar of such quality can play its maximum effect when matrix compounds, and be conducive to bulb of thunberg fritillary bulb
Seedling.In addition, the bamboo vinegar of the present invention can effectively kill harmful bacteria, the relatively low miscellaneous bacteria rate of matrix is controlled.
3rd, the activated carbon that retort is generated at 700 DEG C or more mixes distillation with crude bamboo vinegar, on the one hand can adsorb thick
Harmful substance and impurity in bamboo vinegar processed, on the other hand can effectively improve gained refined bamboo vinegar pH, adjusted to
PH=3.4~4.8, avoid refined bamboo vinegar peracid, so in compound process by the pH of matrix it is too fast be reduced to reasonable value with
Under, simultaneously so that refined bamboo vinegar retains ammonium ions more as possible, reduces the loss late of nitrogen.
4th, the habit grown according to bulb of thunberg fritillary, it is desirable that growing environment slant acidity, nutrient content are high, can by granulating technique,
Matrix unit weight is controlled in 1.15~1.27g/cm3, pH=5~5.8 can ensure good fertilizer conservation water storage performance, to promote squama
Stem-root.
Description of the drawings
Fig. 1 is the preparation system structure diagram of the present invention；
Wherein, 1 is retort, and 11 be gas outlet, and 12 be bamboo charcoal discharge port, and 13 be activated carbon discharge nozzle, and 14 be pressure reducing valve,
2 be tray, and 3 be the first condenser, and 31 be leakage fluid dram I, and 32 be exhaust outlet, and 4 be the second condenser, and 41 be leakage fluid dram II, and 5 are
Distilling apparatus, 6 be refined bamboo vinegar reception device, and 7 be condensed water, and 8 be condensation pipe.
Specific embodiment
The present invention will be further elaborated with reference to the accompanying drawings and examples, it should which explanation, the description below is only
It is to explain the present invention, its content is not defined.
Embodiment 1：
As shown in Figure 1, a kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort 1 connects the gas outlet of retort 1
11 and condensing plant, condensing plant is opened, closes bamboo charcoal discharge port 12 and activated carbon discharge nozzle 13, with the heating speed of 0.1 DEG C/s
Rate heats material temperature to 250 DEG C, charing process 15 minutes in this temperature range, the condensed equipment condensation of bamboo vinegar steam stream of generation
For crude bamboo vinegar, and the bottom for passing through condensing plant is expelled to distilling apparatus 5；
(2) continue to heat material temperature to 300 DEG C, open bamboo charcoal discharge port 12, the bamboo charcoal of discharge is collected using tray 2, and
Tile cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray 2, until in retort 1
Residual mass is the 1/20 of input amount, closes bamboo charcoal discharge port 12；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon in retort 1, connects activated carbon
Discharge nozzle 13 makes activated carbon slowly enter the distilling apparatus 5 for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes
Condensing plant exports, and avoids flowing back；
(5) distilling apparatus 5 is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, generation
The condensed conduit 8 of steam enters refined bamboo vinegar reception device 6 after condensing, and stands 24 hours, and filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
It is pico- to open pressure reducing valve 14 in step (1), for adjusting pressure in retort 1；In step (3), close bamboo charcoal and go out
Pressure reducing valve 14 is also turn off while material mouth 12.
In step (1), the bamboo vinegar steam of generation, respectively will be cold from the bottom of two condensers followed by two condensers
Solidifying obtained crude bamboo vinegar is expelled to distilling apparatus 5.
In step (4), in distilling apparatus 5, the mass ratio of activated carbon and crude bamboo vinegar is 1：12.
In step (5), the pH=3.4 of refined bamboo vinegar.
The specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 3 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5, stop sprinkling bamboo vinegar to get.
In step (6-2), thickness of earth covering is 1cm on hay.
In step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：8.
The whole-process control moisture in the preparation process of cultivation matrix, the moisture weight content of final gained cultivation matrix are less than
15%.
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
The corresponding a kind of preparation system of bulb of thunberg fritillary plantation substrate of above-mentioned preparation process, including bamboo charcoal preparation facilities and bamboo
Vinegar liquid preparation facilities two parts, bamboo charcoal preparation facilities are retort 1, and the main body of bamboo vinegar preparation facilities is condensing plant, is carbonized
The top and bottom of stove 1 are respectively equipped with gas outlet 11 and bamboo charcoal discharge port 12, and the lower section of bamboo charcoal discharge port 12 sets tray 2,
Gas outlet 11 is connected to the top of condensing plant, and the bottom of condensing plant is connected with distilling apparatus 5；The bottom of retort 1 is also set
Active charcoal discharge nozzle 13, activated carbon discharge nozzle 13 are connected to distilling apparatus 5；Distilling apparatus 5 passes through condensation pipe 8 and refined bamboo
Vinegar liquid reception device 6 connects.
The bottom of retort 1 is additionally provided with pressure reducing valve 14, and the bamboo vinegar steam that being arranged on bottom can prevent passes through pressure reducing valve
14 lose.
Condensing plant includes the first condenser 3 and the second condenser 4 of series connection, and the gas outlet 11 of retort 1 is connected to the
The top of one condenser 3, the bottom of the first condenser 3 are equipped with leakage fluid dram I 31 and exhaust outlet 32,32 and second condenser of exhaust outlet
4 top connection, the bottom of the second condenser 4 are equipped with leakage fluid dram II 41, and leakage fluid dram I 31 and leakage fluid dram II 41 are respectively connected to steam
Distillation unit 5.
The outside of first condenser 3 and the second condenser 4 is respectively arranged the first condensing water conduit and the second condensing water conduit,
Condensed water 7 enters from the bottom of the second condensing water conduit, top outflow, then flows into the bottom of the first condensing water conduit, finally
It is flowed out via the top of the first condensing water conduit.
The material of tray 2 is stainless steel, is conducive to collected bamboo charcoal tiling heat dissipation.
Stirring rod is equipped in distilling apparatus 5.
Embodiment 2：
As shown in Figure 1, a kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort 1 connects the gas outlet of retort 1
11 and condensing plant, condensing plant is opened, closes bamboo charcoal discharge port 12 and activated carbon discharge nozzle 13, with the heating speed of 0.1 DEG C/s
Rate heats material temperature to 350 DEG C, charing process 20 minutes in this temperature range, the condensed equipment condensation of bamboo vinegar steam stream of generation
For crude bamboo vinegar, and the bottom for passing through condensing plant is expelled to distilling apparatus 5；
(2) continue to heat material temperature to 350 DEG C, open bamboo charcoal discharge port 12, the bamboo charcoal of discharge is collected using tray 2, and
Tile cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray 2, until in retort 1
Residual mass is the 1/20 of input amount, closes bamboo charcoal discharge port 12；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon in retort 1, connects activated carbon
Discharge nozzle 13 makes activated carbon slowly enter the distilling apparatus 5 for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes
Condensing plant exports, and avoids flowing back；
(5) distilling apparatus 5 is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, generation
The condensed conduit 8 of steam enters refined bamboo vinegar reception device 6 after condensing, and stands 24 hours, and filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
It is pico- to open pressure reducing valve 14 in step (1), for adjusting pressure in retort 1；In step (3), close bamboo charcoal and go out
Pressure reducing valve 14 is also turn off while material mouth 12.
In step (1), the bamboo vinegar steam of generation, respectively will be cold from the bottom of two condensers followed by two condensers
Solidifying obtained crude bamboo vinegar is expelled to distilling apparatus 5.
In step (4), in distilling apparatus 5, the mass ratio of activated carbon and crude bamboo vinegar is 1：12.
In step (5), the pH=4.8 of refined bamboo vinegar.
The specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 3 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 5 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5.8, stop sprinkling bamboo vinegar to get.
In step (6-2), thickness of earth covering is 1cm on hay.
In step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：8.
The whole-process control moisture in the preparation process of cultivation matrix, the moisture weight content of final gained cultivation matrix are less than
15%.
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
The corresponding a kind of preparation system of bulb of thunberg fritillary plantation substrate of above-mentioned preparation process, including bamboo charcoal preparation facilities and bamboo
Vinegar liquid preparation facilities two parts, bamboo charcoal preparation facilities are retort 1, and the main body of bamboo vinegar preparation facilities is condensing plant, is carbonized
The top and bottom of stove 1 are respectively equipped with gas outlet 11 and bamboo charcoal discharge port 12, and the lower section of bamboo charcoal discharge port 12 sets tray 2,
Gas outlet 11 is connected to the top of condensing plant, and the bottom of condensing plant is connected with distilling apparatus 5；The bottom of retort 1 is also set
Active charcoal discharge nozzle 13, activated carbon discharge nozzle 13 are connected to distilling apparatus 5；Distilling apparatus 5 passes through condensation pipe 8 and refined bamboo
Vinegar liquid reception device 6 connects.
The bottom of retort 1 is additionally provided with pressure reducing valve 14, and the bamboo vinegar steam that being arranged on bottom can prevent passes through pressure reducing valve
14 lose.
Condensing plant includes the first condenser 3 and the second condenser 4 of series connection, and the gas outlet 11 of retort 1 is connected to the
The top of one condenser 3, the bottom of the first condenser 3 are equipped with leakage fluid dram I 31 and exhaust outlet 32,32 and second condenser of exhaust outlet
4 top connection, the bottom of the second condenser 4 are equipped with leakage fluid dram II 41, and leakage fluid dram I 31 and leakage fluid dram II 41 are respectively connected to steam
Distillation unit 5.
The outside of first condenser 3 and the second condenser 4 is respectively arranged the first condensing water conduit and the second condensing water conduit,
Condensed water 7 enters from the bottom of the second condensing water conduit, top outflow, then flows into the bottom of the first condensing water conduit, finally
It is flowed out via the top of the first condensing water conduit.
The material of tray 2 is stainless steel, is conducive to collected bamboo charcoal tiling heat dissipation.
Stirring rod is equipped in distilling apparatus 5.
Embodiment 3：
As shown in Figure 1, a kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort 1 connects the gas outlet of retort 1
11 and condensing plant, condensing plant is opened, closes bamboo charcoal discharge port 12 and activated carbon discharge nozzle 13, with the heating speed of 0.1 DEG C/s
Rate heats material temperature to 300 DEG C, charing process 18 minutes in this temperature range, the condensed equipment condensation of bamboo vinegar steam stream of generation
For crude bamboo vinegar, and the bottom for passing through condensing plant is expelled to distilling apparatus 5；
(2) continue to heat material temperature to 320 DEG C, open bamboo charcoal discharge port 12, the bamboo charcoal of discharge is collected using tray 2, and
Tile cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray 2, until in retort 1
Residual mass is the 1/20 of input amount, closes bamboo charcoal discharge port 12；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon in retort 1, connects activated carbon
Discharge nozzle 13 makes activated carbon slowly enter the distilling apparatus 5 for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes
Condensing plant exports, and avoids flowing back；
(5) distilling apparatus 5 is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, generation
The condensed conduit 8 of steam enters refined bamboo vinegar reception device 6 after condensing, and stands 24 hours, and filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
It is pico- to open pressure reducing valve 14 in step (1), for adjusting pressure in retort 1；In step (3), close bamboo charcoal and go out
Pressure reducing valve 14 is also turn off while material mouth 12.
In step (1), the bamboo vinegar steam of generation, respectively will be cold from the bottom of two condensers followed by two condensers
Solidifying obtained crude bamboo vinegar is expelled to distilling apparatus 5.
In step (4), in distilling apparatus 5, the mass ratio of activated carbon and crude bamboo vinegar is 1：12.
In step (5), the pH=4 of refined bamboo vinegar.
The specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 4 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5.5, stop sprinkling bamboo vinegar to get.
In step (6-2), thickness of earth covering is 1cm on hay.
In step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：8.
The whole-process control moisture in the preparation process of cultivation matrix, the moisture weight content of final gained cultivation matrix are less than
15%.
Step (6-4) is also granulated after stopping spraying bamboo vinegar, controls the unit weight ranging from 1.2g/ of cultivation matrix
cm3。
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
The corresponding a kind of preparation system of bulb of thunberg fritillary plantation substrate of above-mentioned preparation process, including bamboo charcoal preparation facilities and bamboo
Vinegar liquid preparation facilities two parts, bamboo charcoal preparation facilities are retort 1, and the main body of bamboo vinegar preparation facilities is condensing plant, is carbonized
The top and bottom of stove 1 are respectively equipped with gas outlet 11 and bamboo charcoal discharge port 12, and the lower section of bamboo charcoal discharge port 12 sets tray 2,
Gas outlet 11 is connected to the top of condensing plant, and the bottom of condensing plant is connected with distilling apparatus 5；The bottom of retort 1 is also set
Active charcoal discharge nozzle 13, activated carbon discharge nozzle 13 are connected to distilling apparatus 5；Distilling apparatus 5 passes through condensation pipe 8 and refined bamboo
Vinegar liquid reception device 6 connects.
The bottom of retort 1 is additionally provided with pressure reducing valve 14, and the bamboo vinegar steam that being arranged on bottom can prevent passes through pressure reducing valve
14 lose.
Condensing plant includes the first condenser 3 and the second condenser 4 of series connection, and the gas outlet 11 of retort 1 is connected to the
The top of one condenser 3, the bottom of the first condenser 3 are equipped with leakage fluid dram I 31 and exhaust outlet 32,32 and second condenser of exhaust outlet
4 top connection, the bottom of the second condenser 4 are equipped with leakage fluid dram II 41, and leakage fluid dram I 31 and leakage fluid dram II 41 are respectively connected to steam
Distillation unit 5.
The outside of first condenser 3 and the second condenser 4 is respectively arranged the first condensing water conduit and the second condensing water conduit,
Condensed water 7 enters from the bottom of the second condensing water conduit, top outflow, then flows into the bottom of the first condensing water conduit, finally
It is flowed out via the top of the first condensing water conduit.
The material of tray 2 is stainless steel, is conducive to collected bamboo charcoal tiling heat dissipation.
Stirring rod is equipped in distilling apparatus 5.
Comparative example 1
A kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) air-dried high mountain mao bamboon is put into retort, connects gas outlet and the condensing plant of retort, opened condensation and set
It is standby, bamboo charcoal discharge port and activated carbon discharge nozzle are closed, material temperature is heated to 300 DEG C with the heating rate of 0.1 DEG C/s, in this temperature model
Enclose interior charing process 18 minutes, the condensed equipment of bamboo vinegar steam stream of generation is condensed into crude bamboo vinegar, and pass through condensing plant
Bottom be expelled to distilling apparatus；
(2) continue to heat material temperature to 320 DEG C, open bamboo charcoal discharge port, the bamboo charcoal of discharge is collected using tray, and tile
Cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray, until residual in retort
1/20 that quality is input amount is stayed, closes bamboo charcoal discharge port；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon in retort, connects activated carbon
Discharge nozzle makes activated carbon slowly enter the distilling apparatus for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes condensation
Equipment exports, and avoids flowing back；
(5) distilling apparatus is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, generation
Enter refined bamboo vinegar reception device after the condensed conduit condensation of steam, stand 24 hours, filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
In step (1), pressure reducing valve is opened slightly, for adjusting pressure in retort；In step (3), bamboo charcoal discharging is closed
Pressure reducing valve is also turn off while mouth.
In step (1), the bamboo vinegar steam of generation, respectively will be cold from the bottom of two condensers followed by two condensers
Solidifying obtained crude bamboo vinegar is expelled to distilling apparatus.
In step (4), in distilling apparatus, the mass ratio of activated carbon and crude bamboo vinegar is 1：12.
In step (5), the pH=4 of refined bamboo vinegar.
The specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 4 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5.5, stop sprinkling bamboo vinegar to get.
In step (6-2), thickness of earth covering is 1cm on hay.
In step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：8.
The whole-process control moisture in the preparation process of cultivation matrix, the moisture weight content of final gained cultivation matrix are less than
15%.
Step (6-4) is also granulated after stopping spraying bamboo vinegar, controls the unit weight ranging from 1.2g/ of cultivation matrix
cm3。
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
Comparative example 2
A kind of preparation process of bulb of thunberg fritillary plantation substrate, is as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort, connect the gas outlet of retort with
Condensing plant opens condensing plant, closes bamboo charcoal discharge port and activated carbon discharge nozzle, and material is heated with the heating rate of 0.1 DEG C/s
Temperature is to 300 DEG C, charing process 18 minutes in this temperature range, and the condensed equipment of bamboo vinegar steam stream of generation is condensed into crude bamboo
Vinegar liquid, and the bottom for passing through condensing plant is expelled to distilling apparatus；
(2) continue to heat material temperature to 320 DEG C, open bamboo charcoal discharge port, the bamboo charcoal of discharge is collected using tray, and tile
Cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray, until residual in retort
1/20 that quality is input amount is stayed, closes bamboo charcoal discharge port；
(4) condensing plant outlet is closed, avoids flowing back；
(5) distilling apparatus is warming up to 120 DEG C, and entering refined bamboo vinegar after the condensed conduit condensation of steam of generation receives dress
It puts, stands 24 hours, filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary as primary raw material with refined bamboo vinegar obtained by step (5) using bamboo charcoal obtained by step (3)
Plantation substrate.
In step (1), pressure reducing valve is opened slightly, for adjusting pressure in retort；In step (3), bamboo charcoal discharging is closed
Pressure reducing valve is also turn off while mouth.
In step (1), the bamboo vinegar steam of generation, respectively will be cold from the bottom of two condensers followed by two condensers
Solidifying obtained crude bamboo vinegar is expelled to distilling apparatus.
The specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 4 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, standby
With；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), is then spread evenly
Mineral powders obtained by step (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar while stirring, measure simultaneously
The pH of system, until pH=5.5, stop sprinkling bamboo vinegar to get.
In step (6-2), thickness of earth covering is 1cm on hay.
In step (6-4), the mass ratio of mineral powders, bamboo charcoal powder and scorched clay dust powder is 1：4：8.
The whole-process control moisture in the preparation process of cultivation matrix, the moisture weight content of final gained cultivation matrix are less than
15%.
Step (6-4) is also granulated after stopping spraying bamboo vinegar, controls the unit weight ranging from 1.2g/ of cultivation matrix
cm3。
A kind of bulb of thunberg fritillary plantation substrate, is obtained by above-mentioned preparation process.
Comparative example 3
A kind of cultivation matrix is according to mass ratio 4 by bamboo charcoal powder and scorched clay dust powder：8 are obtained by mixing.The preparation of bamboo charcoal powder
Method：Bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2 hours, obtain bamboo charcoal powder.The preparation method of scorched clay dust powder：It utilizes
The soil of hay overlying 1cm thickness, with fiery smoke curing into scorched clay dust, 105 DEG C dry 4 hours, cross 40 mesh sieve, obtain scorched clay dust powder.
Test example
The cultivation matrix for preparing Examples 1 to 3 or comparative example 1~3 carries out bulb of thunberg fritillary bulb nursery, and specific method is：10
In the last ten-days period moon, bulb of thunberg fritillary bulb (diameter 3cm) is embedded in cultivation matrix, institute's buried depth degree is 6cm, and seedling raise period is 15 days.It investigates and plants
It trains the miscellaneous bacteria rate of matrix and carries out the emergence rate of bulb of thunberg fritillary bulb nursery using it, the results are shown in Table 1.
The miscellaneous bacteria rate of 1. cultivation matrix of table and the emergence rate using its progress bulb of thunberg fritillary bulb nursery
| Miscellaneous bacteria rate (%) | Emergence rate (%) | |
| Embodiment 1 | ≤0.5 | 97 |
| Embodiment 2 | ≤0.5 | 97 |
| Embodiment 3 | ≤0.5 | 99 |
| Comparative example 1 | ≤0.5 | 85 |
| Comparative example 2 | 12 | 83 |
| Comparative example 3 | 25 | 65 |
As shown in Table 1, the cultivation matrix of Examples 1 to 3 has relatively low miscellaneous bacteria rate, and bulb of thunberg fritillary bulb nursery is carried out using it
Emergence rate it is high.Comparative example 1 omits cow dung, and emergence rate is substantially reduced；Comparative example 2, which omits, to be generated activated carbon and is conducted into
The step of crude bamboo vinegar, the miscellaneous bacteria rate of cultivation matrix significantly rise, and it is apparent to carry out the emergence rate of bulb of thunberg fritillary bulb nursery using it
It reduces；The cultivation matrix of comparative example 3 is not added with bamboo charcoal and bamboo vinegar, and miscellaneous bacteria rate and emergence rate two indices are undesirable.
Above-mentioned, although the foregoing specific embodiments of the present invention is described with reference to the accompanying drawings, not protects model to the present invention
The limitation enclosed, based on the technical solutions of the present invention, those skilled in the art are not needed to make the creative labor and can be done
The various modifications or changes gone out are still within protection scope of the present invention.
Claims (9)
1. a kind of preparation process of bulb of thunberg fritillary plantation substrate, which is characterized in that be as follows：
(1) by air-dried high mountain mao bamboon and cow dung according to mass ratio 8：1 input retort, connects gas outlet and the condensation of retort
Equipment opens condensing plant, closes bamboo charcoal discharge port and activated carbon discharge nozzle, with the heating rate heating material temperature of 0.1 DEG C/s extremely
250~350 DEG C, charing process 15~20 minutes in this temperature range, the condensed equipment of bamboo vinegar steam stream of generation is condensed into
Crude bamboo vinegar, and the bottom for passing through condensing plant is expelled to distilling apparatus；
(2) continue to heat material temperature to 300~350 DEG C, open bamboo charcoal discharge port, the bamboo charcoal of discharge is collected using tray, and put down
Spread cooling；
(3) continue to heat material temperature to 400 DEG C, and weigh the quality of collected bamboo charcoal in tray, until residual matter in retort
1/20 for input amount is measured, closes bamboo charcoal discharge port；
(4) continue to heat material temperature to 700 DEG C or more, raw material is further cracked into activated carbon, connection activated carbon discharging in retort
Pipe, makes activated carbon slowly enter the distilling apparatus for being connected to crude bamboo vinegar, treats that crude bamboo vinegar collection finishes, closes condensing plant
Outlet, avoids flowing back；
(5) distilling apparatus is warming up to 120 DEG C, is come into full contact with by stirring activated carbon with crude bamboo vinegar, the steam of generation
Enter refined bamboo vinegar reception device after condensed conduit condensation, stand 24 hours, filtering is spare；
(6) it compounds to obtain a kind of bulb of thunberg fritillary using bamboo charcoal obtained by step (3) and step (5) gained refined bamboo vinegar as primary raw material special
Cultivation matrix.
2. preparation process according to claim 1, which is characterized in that in step (1), pressure reducing valve is opened slightly, for adjusting
Save pressure in retort；In step (3), pressure reducing valve is also turn off while closing bamboo charcoal discharge port.
3. preparation process according to claim 1, which is characterized in that in step (1), the bamboo vinegar steam of generation followed by
Two condensers are expelled to distilling apparatus from the bottom of two condensers by the crude bamboo vinegar that condensation obtains respectively.
4. preparation process according to claim 1, which is characterized in that the specific method of step (6) is as follows：
(6-1) bamboo charcoal drying and crushing crosses 20 mesh sieve, and 100 DEG C dry 2~3 hours, obtain bamboo charcoal powder, spare；
(6-2) using earthing on hay, with fiery smoke curing into scorched clay dust, 105 DEG C dry 3~5 hours, cross 40 mesh sieve, obtain burnt mud
Grey powder, it is spare；
(6-3) is by lime stone and potassium ore with mass ratio 2：3 mixing, crush, and cross 15 mesh sieve, obtain mineral powders, spare；
The bamboo charcoal powder of step (6-1) is uniformly mixed by (6-4) with the scorched clay dust powder of step (6-2), then spreads evenly step
Mineral powders obtained by (6-3), are uniformly mixed, and then uniformly spray refined bamboo vinegar, while measurement system while stirring
PH, until pH=5~5.8, stop sprinkling bamboo vinegar to get.
5. a kind of bulb of thunberg fritillary plantation substrate, which is characterized in that be by preparation work according to any one of claims 1 to 4
What skill obtained.
6. a kind of corresponding preparation system of bulb of thunberg fritillary plantation substrate of preparation process according to any one of claims 1 to 4,
It is characterised in that it includes bamboo charcoal preparation facilities and bamboo vinegar preparation facilities two parts, the bamboo charcoal preparation facilities is retort, bamboo
The main body of vinegar liquid preparation facilities is condensing plant, and gas outlet and bamboo charcoal discharge port, bamboo are respectively equipped at the top and bottom of retort
The lower section setting tray of charcoal discharge port, the gas outlet is connected to the top of condensing plant, the bottom of condensing plant and distillation
Device connects；The bottom of the retort is additionally provided with activated carbon discharge nozzle, and activated carbon discharge nozzle is connected to distilling apparatus；The steaming
Distillation unit is connect by condensation pipe with refined bamboo vinegar reception device.
7. preparation system according to claim 6, which is characterized in that the bottom of the retort is additionally provided with pressure reducing valve.
8. preparation system according to claim 6, which is characterized in that the condensing plant includes the first condenser of series connection
With the second condenser, the gas outlet of retort is connected to the top of the first condenser, and the bottom of the first condenser is equipped with leakage fluid dram I
And exhaust outlet, exhaust outlet are connect with the top of the second condenser, the bottom of the second condenser is equipped with leakage fluid dram II, the drain
Mouth I and leakage fluid dram II are respectively connected to distilling apparatus.
9. preparation system according to claim 8, which is characterized in that the outside of first condenser and the second condenser
The first condensing water conduit and the second condensing water conduit are respectively arranged, condensed water enters from the bottom of the second condensing water conduit, top
Outflow then flows into the bottom of the first condensing water conduit, is finally flowed out via the top of the first condensing water conduit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810100209.3A CN108243900B (en) | 2018-02-01 | 2018-02-01 | Special cultivation medium for fritillaria thunbergii, preparation process and system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810100209.3A CN108243900B (en) | 2018-02-01 | 2018-02-01 | Special cultivation medium for fritillaria thunbergii, preparation process and system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108243900A true CN108243900A (en) | 2018-07-06 |
| CN108243900B CN108243900B (en) | 2020-04-21 |
Family
ID=62743508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810100209.3A Active CN108243900B (en) | 2018-02-01 | 2018-02-01 | Special cultivation medium for fritillaria thunbergii, preparation process and system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108243900B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0931468A (en) * | 1995-07-20 | 1997-02-04 | Shin Meiwa Ind Co Ltd | Carbonizing device |
| JP2002079229A (en) * | 2000-09-07 | 2002-03-19 | Takeyuki Shima | System for converting carbide and dried product obtained from industrial wastes or the like into resources and system for treating used resources |
| CN103772026A (en) * | 2014-01-13 | 2014-05-07 | 陈温福 | Charcoal-based rice seedling substrate and preparation method thereof |
| CN105622267A (en) * | 2015-12-30 | 2016-06-01 | 聚光科技(杭州)股份有限公司 | Preparation method of novel biological carbon material |
| CN106185877A (en) * | 2016-09-12 | 2016-12-07 | 杨二冰 | The technique of a kind of bamboo charcoal production and device |
| CN206895387U (en) * | 2017-07-13 | 2018-01-19 | 沈阳农业大学 | A kind of charcoal rice nursery substrate production system |
-
2018
- 2018-02-01 CN CN201810100209.3A patent/CN108243900B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0931468A (en) * | 1995-07-20 | 1997-02-04 | Shin Meiwa Ind Co Ltd | Carbonizing device |
| JP2002079229A (en) * | 2000-09-07 | 2002-03-19 | Takeyuki Shima | System for converting carbide and dried product obtained from industrial wastes or the like into resources and system for treating used resources |
| CN103772026A (en) * | 2014-01-13 | 2014-05-07 | 陈温福 | Charcoal-based rice seedling substrate and preparation method thereof |
| CN105622267A (en) * | 2015-12-30 | 2016-06-01 | 聚光科技(杭州)股份有限公司 | Preparation method of novel biological carbon material |
| CN106185877A (en) * | 2016-09-12 | 2016-12-07 | 杨二冰 | The technique of a kind of bamboo charcoal production and device |
| CN206895387U (en) * | 2017-07-13 | 2018-01-19 | 沈阳农业大学 | A kind of charcoal rice nursery substrate production system |
Non-Patent Citations (1)
| Title |
|---|
| 卢辛成 等: "木醋液的制备、精制与应用研究进展", 《林产化学与工业》 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108243900B (en) | 2020-04-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Wu et al. | Effects of ridge and furrow rainwater harvesting system combined with irrigation on improving water use efficiency of maize (Zea mays L.) in semi-humid area of China | |
| CN103787732B (en) | A kind of watermelon plug seedling substrate and preparation method thereof | |
| CN102356746B (en) | Technology for cultivating organic fruit and vegetable matrix | |
| CN103755445B (en) | A kind of watermelon plug seedling substrate and application thereof | |
| CN101743891B (en) | Straw-type soilless culture medium and preparation method thereof | |
| CN108865170A (en) | A kind of charcoal base soil structure conditioner preparation method and method of administration | |
| Karam et al. | Influence of genotypes and potassium application rates on yield and potassium use efficiency of potato | |
| CN104909878B (en) | A kind of drought-hit area leaf vegetables cultivation matrix and preparation method thereof | |
| CN103283452B (en) | Radix codonopsis cultivation method | |
| CN107162773A (en) | A kind of rice seedling raising ground substance and preparation method thereof | |
| CN104478591A (en) | Method for preparing lightweight matrix for sky-rise greenery | |
| CN104782463A (en) | Eco-organic type soilless culture technology | |
| CN107466828A (en) | Ecologic planting plate and preparation method and application | |
| CN108887142A (en) | A kind of full nutrition organic ecological soilless culture substrate formula suitable for cucumber | |
| CN103651067A (en) | Soilless turf culturing medium and preparing method of soilless turf culturing medium | |
| CN110066203A (en) | A kind of kudzu charcoal soil conditioner and preparation method thereof | |
| CN105994134A (en) | Method for ecological recirculating breeding of live pigs | |
| Karam et al. | Potato response to potassium application rates and timing under semi-arid conditions | |
| CN105850685A (en) | Vegetable seedling substrate | |
| CN109076915A (en) | A kind of propagation method of Nanchuan lily | |
| CN106561423A (en) | Fermented jerusalem artichoke straw for soilless culture, and composite medium of fermentative jerusalem artichoke straw | |
| CN106866201A (en) | Rice nursery substrate | |
| CN109699424A (en) | A kind of cultural method that checkerberry fertilizer crop cold resistance in Beijing-tianjin-hebei Region is overwintering | |
| CN109874637A (en) | A kind of preparation method of high-efficiency environment friendly seedling medium | |
| CN108353742A (en) | A method of planting crowndaisy chrysanthemum in side slope |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A special culture medium, preparation technology and system for Fritillaria thunbergii Effective date of registration: 20210304 Granted publication date: 20200421 Pledgee: Industrial Bank Co.,Ltd. Shanghai Minhang sub branch Pledgor: SEEK BIO-TECHNOLOGY (SHANGHAI) Co.,Ltd. Registration number: Y2021980001449 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230524 Granted publication date: 20200421 Pledgee: Industrial Bank Co.,Ltd. Shanghai Minhang sub branch Pledgor: SEEK BIO-TECHNOLOGY (SHANGHAI) Co.,Ltd. Registration number: Y2021980001449 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A specialized cultivation substrate, preparation process, and system for Zhejiang shellfish Granted publication date: 20200421 Pledgee: Agricultural Bank of China Limited Shanghai Pudong Branch Pledgor: SEEK BIO-TECHNOLOGY (SHANGHAI) Co.,Ltd. Registration number: Y2024980010691 |