CN107903091A - The pollution treatment of intermittent cyclic tank and the method for system fertilizer consumption organic solid waste pollutant - Google Patents
The pollution treatment of intermittent cyclic tank and the method for system fertilizer consumption organic solid waste pollutant Download PDFInfo
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- CN107903091A CN107903091A CN201711225864.3A CN201711225864A CN107903091A CN 107903091 A CN107903091 A CN 107903091A CN 201711225864 A CN201711225864 A CN 201711225864A CN 107903091 A CN107903091 A CN 107903091A
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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Abstract
A kind of intermittent cyclic tank pollution treatment and the method for system fertilizer consumption organic solid waste pollutant, step are：（1）Organic solid waste pollutant is ground into the solid material of below 5mm sizes；It is 60%~80% to ensure solid material water content；（2）Solid material delivers into harmless treatment device, and temperature is increased to 70~85 DEG C, is kept for 10~30 minutes, carries out harmless treatment；And open emission-control equipment and carry out deodorization operation；After harmless treatment, temperature continuation of insurance holds more than 80 DEG C；When solid material water content is changed into 60~65%, EM bacterium or YM bacterium are added, while it is more than 6 to adjust solid material pH value, adjustment solid material carbon/nitrogen is than 25~30:1；Continue stirring and deodorization operation, when the time is 2~4 small；（3）Solid material obtained above is sent to aerobic fermentation is carried out in aerobic fermentation tank, solid material aerobic fermentation, which reaches curing standard and water content standard, to discharge.This method is handled the organic solid castoff same day that the same day produces, and solves the problem of pollution environment.
Description
Technical field
The invention belongs to the technical field of organic solid castoff recycling, is specifically a kind of intermittent cyclic tank pollution treatment
With the method for system fertilizer consumption organic solid waste pollutant.
Background technology
With economic fast development and increase of the mankind to material requisite amount, organic solid castoff also constantly increases
Organic solid castoff refers to crops residue, animal wastes, domestic sludge, food processing discarded object, industrial organic waste
Thing, timber processing discarded object and house refuse etc. contain the discarded object of abundant organic matter.The annual stalk in China according to statistics
Output breaks through 8 × 108T, and animal waste in 2012 reaches 25.78 × 108T, remaining meal rubbish is also up to 6 × 107T, this
Huge all kinds of organic solid castoffs, generally existing lignocellulosic concentration is high, heavy metal concentration is high, it is more to carry pathogen
The problems such as with foul smelling smell, become serious social concern, it is necessary to expend substantial amounts of human and material resources and financial resources are solved
Certainly, while environment can also be polluted.At present the processing mode of organic solid castoff mainly have burning, landfill, curing and
The several methods such as compost, it is impossible to solve current ecological overall situation pollution of waterhead, soil pollution, air pollution, global warming etc.
Big problem.
All kinds of organic solid castoffs contain abundant organic matter, if carrying out recycling treatment after implementing harmless treatment,
It can reduce environmental pollution and promote recycling for resource, moreover it is possible to realize 100% minimizing.Therefore, pollution treatment fertilizer is that have
The best mode that machine solid waste resource utilizes, pollution treatment fertilizer refer to making using the redox and synthesis capability of microorganism
By organic matter decomposition it is stable humus during fertilizer, simultaneously synthesizing mass efficient state mineral element, forms to environment not structure
Into the process of the organic fertilizer of harm.Since organic solid castoff is all continous way discharge throughout the year, with the high speed of industry
Development and the continuous growth of urban population, the processing pressure of organic solid castoff also constantly increase.How at effective, harmless
Reason organic solid castoff becomes very urgent task.
The content of the invention
The object of the present invention is to provide a kind of intermittent cyclic tank pollution treatment and the side of system fertilizer consumption organic solid waste pollutant
Method；The pollution treatment of this intermittent cyclic tank and the method for system fertilizer consumption organic solid waste pollutant are that comprehensive all kinds of organic substance solids give up
Abandon pollutant pollution treatment fertilizer technology and EM microbial bacterias, configuration production is drafted in YM microbial bacterias process specifications and pool
Equipment and technology, a whole set of intermittent cyclic tank pollution treatment reformulated and the fertile technology of system；The technology is source pollution treatment system
Fertilizer, gets twice the result with half the effort than traditional pollution treatment, be one can undertake the pollution treatment of overall situation high-volume and fertile one new concept of task of system be
System technology.Organic solid castoff fermentation is prepared organic fertilizer by this method, is carried out on the day of the organic solid castoff that the same day produces
Harmless treatment, solves the problems, such as that organic solid castoff largely accumulates pollution environment.
The present invention is realized using following technical scheme：
A kind of intermittent cyclic tank pollution treatment and the method for system fertilizer consumption organic solid waste pollutant, the processing step of use are as follows：
（1）Daily organic solid waste pollutant to be treated is ground into the particle of below 5mm sizes；If organic solid
Waste pollutant particle need to carry out separation of solid and liquid when being wet feed, obtain liquid material and water content as 60%~80% solid material；Liquid
Material is transported into sewage-treatment plant and carries out sewage disposal；Taken plus water if organic solid waste pollutant particle is siccative
Make solid material water content 60%~80%；
（2）Solid material delivers into harmless treatment device, and temperature is increased to 70~85 DEG C, is kept for 10~30 minutes, carries out nothing
Evilization processing；And open the emission-control equipment being connected with harmless treatment device and carry out deodorization operation；After harmless treatment, nothing
Temperature continuation of insurance in evilization processing unit holds more than 80 DEG C and helps to remove the moisture in solid material；When solid material water content is changed into 60
When~65%, EM bacterium or YM bacterium are added, while it is more than 6 to add acidic excipient or basic auxiliary adjustment solid material pH value, addition
Carbon/nitrogen auxiliary material adjustment solid material carbon/nitrogen is than 25~30:1；Continue stirring and deodorization operation, when the time is 2~4 small；
（3）Solid material obtained above is sent to passing through A periods, B periods, C periods and D times in aerobic fermentation tank
Section, using zinc cation+activated carbon absorption processing unit deodorization；Solid material aerobic fermentation reaches curing standard and water content mark
Standard can discharge, the fermentation tank after discharging, that is, reusable.
When adding EM bacterium, the temperature of solid material need to be down to 40~45 DEG C could add EM bacterium.
The additive amount of EM bacterium or YM bacterium is：Each ton of solid material adds 1~1.5 kilogram.
The acidic excipient is one or more of mixing in sulfuric acid, hydrochloric acid and acetic acid；The basic auxiliary is raw
Pulverized limestone.
The carbon/nitrogen auxiliary material is that the one or more in sugarcane marrow, rice bran, molasses, wheat bran, animal dung and peanut press pulp are mixed
Close.
EM bacterium and addition YM bacterium are added in solid material, by A periods, B periods, C periods in aerobic fermentation tank
It is different with the technical parameter of D periods；When adding EM bacterium, the A periods are 0.2~0.3% 40 DEG C of perseverances of injection solid material volume
Warm air, by the temperature of solid material be maintained at 40~45 DEG C, humidity be 60~65%, ventilation time for 24 it is small when, make EM bacterium and solid
Body material obtains optimal organic substance and degrades decomposed fertilizer efficiency and optimal organic substance degraded decomposed period time, and it is every 24 it is small when dynamic
Ferment slow stirring 6~8 times；The B periods are the ventilation degraded decomposed period time very fast period, injection solid material volume
0.1~0.2% 40 DEG C of Tempeerature-constant airs, holding solid material temperature is 40~45 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when dynamic fermentation slow stirring 4~6 times；The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, injection
40 DEG C of Tempeerature-constant airs of the 0.1% of solid material volume, to keep solid material temperature be 40~45 DEG C, humidity is 50~55%, during ventilation
Between for 48 it is small when, and it is every 24 it is small when dynamic fermentation slow stirring 2~4 times；The D periods are the decomposed work of organic matter degradation of solid material
When condition pH value rises to 7.8~8, to reach curing standard, can implement the D periods dries operation, and the 0.2 of injection solid material volume
65 DEG C of~0.3% wait warm air, and Fast Persistence stirring dehumidifies, and when drying time is about 16 small, reaches water content 30%
Discharging.When adding YM bacterium, the A periods are 60 DEG C of Tempeerature-constant airs of 0.2~0.3% times of amount of injection solid material volume, by solid material
Temperature be maintained at 60~65 DEG C, humidity remain 60~65%, ventilation time for 24 it is small when, YM bacterium and solid material is obtained most
Fast organic substance is degraded decomposed speed and optimal organic substance degraded decomposed period time, and it is every 24 it is small when dynamic fermentation slowly turn over
Material 6~8 times；The B periods are ventilation degraded decomposed period time very fast period, the 0.1~0.2% of injection solid material volume
60 DEG C of Tempeerature-constant airs, to keep solid material temperature be 60~65 DEG C, humidity is 55~60%, ventilation time for 48 it is small when, it is and every 24 small
When dynamic fermentation slow stirring 4~6 times；The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, injection solid material volume
0.1% 60 DEG C of Tempeerature-constant airs, holding solid material temperature is 60~65 DEG C, humidity is 50~55%, when ventilation time is 48 small, and
It is every 24 it is small when dynamic fermentation slow stirring 2~4 times；The D periods rise to 7.8 for the decomposed operating mode pH value of organic matter degradation of solid material
When~8, to reach curing standard, can implement the D periods dries operation, 65 DEG C of 0.2~0.3% of injection solid material volume
Deng warm air, and Fast Persistence stirring dehumidifies, and when drying time is about 16 small, reaching water content 30% can discharge.
Solid material can also add ventilative auxiliary material when delivering into harmless treatment device, the ventilative auxiliary material is stalk
The mixture of one or both of particle and sawdust；Stalk particle is the particle that below 5mm sizes are ground into using stalk；Thoroughly
The additive amount of wind auxiliary material accounts for the 20~30% of gross weight.When ventilative auxiliary material is added with solid material, addition EM bacterium and addition YM bacterium,
It is different by the technical parameter of A periods, B periods, C periods and D periods in aerobic fermentation tank；During addition EM bacterium
The A periods are 0.2~0.3% 40 DEG C of Tempeerature-constant airs of injection solid material volume, and the temperature of solid material is maintained at 40~45
DEG C, humidity be 60~65%, ventilation time for 24 it is small when, EM bacterium and solid material is obtained optimal organic substance and degrade decomposed fertilizer efficiency
Degrade the decomposed period time with optimal organic substance, and it is every 24 it is small when static fermentation stirring 3~4 times；The B periods degrade for ventilation
The decomposed period time very fast period, injects 0.1~0.2% 40 DEG C of Tempeerature-constant airs of solid material volume, keeps solid material temperature
Be 55~60% for 40~45 DEG C, humidity, ventilation time for 48 it is small when, and it is every 24 it is small when static fermentation stirring 2~3 times；The C times
Section is degraded decomposed fertilizer efficiency stabilization time section for ventilation, is injected 0.1% 40 DEG C of Tempeerature-constant airs of solid material volume, is kept solid material
Temperature is 40~45 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when static fermentation stirring 1~2 time；D
When period rises to 7.8~8 for the decomposed operating mode pH value of organic matter degradation of solid material, to reach curing standard, when can implement D
Between section drying operation, 65 DEG C of 0.2~0.3% of injection solid material volume wait warm airs, and quick 6~8 times lasting stirrings remove
Wet, when drying time is about 16 small, reaching water content 30% can discharge.A periods when adding YM bacterium are injection solid material body
60 DEG C of Tempeerature-constant airs of long-pending 0.2~0.3% times of amount, by the temperature of solid material be maintained at 60~65 DEG C, humidity remain 60~
65%, when ventilation time is 24 small, YM bacterium and solid material is obtained the most fast organic substance decomposed speed of degraded and optimal organic substance
Degrade the decomposed period time, and it is every 24 it is small when static fermentation stirring 3~4 times；The B periods for ventilation degraded the decomposed period time compared with
The fast period, injects 0.1~0.2% 60 DEG C of Tempeerature-constant airs of solid material volume, keep solid material temperature for 60~65 DEG C, it is wet
Spend for 55~60%, ventilation time for 48 it is small when, and it is every 24 it is small when static fermentation stirring 2~3 times；The C periods are rotten for ventilation degraded
Ripe fertilizer efficiency stabilization time section, injects 0.1% 60 DEG C of Tempeerature-constant airs of solid material volume, keep solid material temperature for 60~65 DEG C,
Humidity is 50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when static fermentation stirring 1~2 time；The D periods are solid material
When the decomposed operating mode pH value of organic matter degradation rises to 7.8~8, to reach curing standard, can implement the D periods dries operation, notes
Enter the 0.2~0.3% of solid material volume 65 DEG C wait warm air, and continue stirring dehumidifying, when drying time is about 16 small, reach
Water content 30% can discharge.The material of discharge is as organic fertilizer.
Our legal system fertilizer is aerobic fermentation mode, and technological requirement will keep certain oxygen content amount, and general technology requirement will add
Add 20~30% ventilative stones, this technique is defined as static aerobic fermentation；Some places do not have ventilative auxiliary material, this technique is used and stirred
Mix the slow mobile material of device and produce gap, to help material to improve aerobic fermentation, be defined as dynamic aerobic fermentation.
The exhaust-gas treatment of the present invention, it is plasma deodorizing apparatus that harmless treatment section, which uses,；Solid fermentation section is washed using biology
+ activated carbon absorption processing unit is washed, can be according to treating capacity installation purchased in market.The plasma deodorizing apparatus that the present invention uses is in Jiangsu
Ai Yijia Electronic Science and Technology Co., Ltd.s buy, address：Jiangsu Province Yixing City Gao Cheng Zhen Xin village road 18；The biology that the present invention uses
Washing+activated carbon absorption processing unit is bought in Jiangsu Taicang Yi Sheng chemical anticorrosions Co., Ltd, address:Jiangsu is too
Northern 204 national highways in the straight pool of storehouse city Shaxi Town are close to.Harmless treatment device is that one end can be fed, and the other end is arranged by plasma deodorizing apparatus
Wind deodorization, and the internal equipment for being provided with agitating device and heating unit.
EM bacterium be 10 based on photosynthetic bacteria, lactic acid bacteria, saccharomycete and actinomyces belong to more than 80 microorganisms it is compound and
Into a kind of micro- life bacteria preparation.The mechanism of action is to form the competition of EM bacterium and pathogenic microorganism contention nutrition, since EM bacterium exist
Easily lived and reproduced in fermentation mixture, so the ecologic niche in fermentation mixture can comparatively fast and be stably occupied, formed with
The advantage group of the microbial bacteria of benefit, so as to control the breeding of pathogenic microorganism, can effectively degrade admittedly for 40~45 DEG C in temperature
The decomposed system fertilizer of organic matter of body material, fertilizer efficiency are notable and energy saving.YM bacterium are a kind of hyperthermophilic microorganisms, are grown at 70~85 DEG C
It is active, it can effectively ferment and decompose the aerobic microorganism of all organic wastes, available for municipal sewage plant and city rubbish
The Sludge Composting of rubbish Treatment stations and agriculture crop field organic waste fertilizer etc., innoxious, minimizing, stabilisation and recycling effect
Significantly.The EM bacterium and YM bacterium that the present invention uses can be bought in Asia environmental protection Pty Ltd, address：Jiangsu Province Yixing City dragon
Pond road 35.
The intermittent cyclic tank pollution treatment of the present invention and the method for system fertilizer consumption organic solid waste pollutant, are that will need to handle
Organic solid waste pollutant be sent into harmless treatment device implement harmless treatment, then be sent into solid-state fermentation tank be prepared as it is organic
Fertilizer.Pollution treatment is run with the fertile overall process of system in enclosed type equipment, and no waste residue, waste water, exhaust gas overflow；Waste water is through simultaneous oxygen membrane bioreaction
Device is answered to handle qualified discharge.Organic solid waste pollutant harmless treatment standard presses national [the harmless treatment technology of feces of livestock and poultry
Codes and standards] NYT-2006 execution；Biological organic fertilizer standard presses Minister Agriculture of China's industry [biological organic fertilizer standard]
NY525-202 and [biological organic fertilizer standard] NY848-202 is performed.Organic solid waste pollutant harmless treatment temperature
It is set to 70~85 DEG C；Organic solid waste pollutant system fertilizer is aerobic fermentation mode；Select domestic ripe microorganism EM bacterium or
Microorganism YM bacterium and its aerobic fermentation process；EM bacterium aerobic fermentation degraded organic matter optimal temperature is 40~45 DEG C；Mixture
Humidity is 50~65%；PH value more than 6；Carbon/nitrogen ratio (C/N) is 25~30:In the range of 1；Oxygen content amount for volume of material 0.1~
0.2 times of amount；The aerobic fermentation degraded organic matter time is 5~7 days (5 days fixed)；Production cycle for 6 days totally 144 it is small when.YM bacterium are aerobic
Fermentative degradation organic matter optimal temperature is 65~85 DEG C；Mixture humidity is 50~65%；PH value more than 6；Carbon/nitrogen ratio (C/N)
25~30:In the range of 1；Oxygen content amount is 0.1~0.3 times of amount of volume of material；The aerobic fermentation degraded organic matter time is 5~7
My god (fixed 5 days)；Production cycle for 6 days totally 144 it is small when.The present invention the interval meaning of word be it is discontinuous, here implication be phase every two days
Or be separated by 24 it is small when；The circulating tank meaning of word is the tank of circulation, is+5 operation circulating tank cycle operations of 1 non-conservation tank here,
Be 5+1 weeks robin, i.e., daily the one degraded decomposed time of one non-conservation tank of charging and discharging daily up to 120 it is small when run tank,
It is the intermittent cyclic tank Sequential Production in 6 day time to realize in the production cycle.Tank implication is unit tank, both represents body
Shape, and metering is represented, it is prior still to represent an inventive technique, standardized technique, standard volume technology are formd in tank
With the loop control technology that the production cycle is 6 days；One group of module pollution treatment can realize consumption organic solid with fertilizer producing system and give up
Pollutant 1.5~750m3/ tanks day is abandoned, realizes and prepares organic 1.0~500 tons/tank of curing fertilizer day.
Intermittent cyclic tank periodic duty process:Within six days circulating tank periodic duty time, first circulating tank cycle,
The harmless mixture handled well is fed toward 1~No. 5 solid-state fermentation tank in order daily, and carries out above-mentioned cycle A~D periods
Operation.Second first day circulating tank cycle, No. 1 solid-state fermentation tank A~D periods periodic duty full 120 discharge when small, take turns
For non-conservation tank；No. 6 solid-state fermentation tank chargings, and carry out above-mentioned A~D periods periodic duty.Second day, No. 2 solid-state fermentation tank A
~D periods periodic duty full 120 discharges when small, takes turns as non-conservation tank；The charging of No. 1 solid-state fermentation tank, and when carrying out above-mentioned A~D
Between section periodic duty.3rd day, No. 3 solid-state fermentation tank A~D periods periodic duties full 120 discharged when small, take turns as non-conservation tank；2
The charging of number solid-state fermentation tank, and carry out above-mentioned A~D periods periodic duty.4th day, No. 4 solid-state fermentation tank A~D periods
Periodic duty full 120 discharges when small, takes turns as non-conservation tank；No. 3 solid-state fermentation tank chargings, and carry out above-mentioned cycle A~D periods fortune
OK.5th day, No. 5 solid-state fermentation tank A~D periods periodic duties full 120 discharged when small, take turns as non-conservation tank；No. 4 solid fermentations
Tank is fed, and carries out above-mentioned A~D periods periodic duty.6th day, No. 6 solid-state fermentation tank A~D period periodic duties were expired
120 discharge when small, take turns as non-conservation tank；No. 1 solid-state fermentation tank charging, and carry out above-mentioned A~D periods periodic duty.From the 3rd
Cycle starts the cycle over first and second periodic duty, six solid-state fermentation tank intermittent cyclic Reusabilities.
This method capital equipment uses 1 group of harmless processor, realizes to the standardization of organic solid waste pollutant
Harmless processing；Realize dispensing and the mixing of supplementary material standard volume；Realize the harmless processing of organic solid waste pollutant and original
Auxiliary material dispensing and the normalized temporal of mixing.
This method capital equipment uses 6 solid-state fermentation tanks, implements 5+1 weeks robin and recycles, realizes intermittent
Sequential Production, that is to say the normalized temporal for realizing organic solid waste pollutant aerobic fermentation system fertilizer；Realize pair
The running technology of standardization and the control technology of standard volume of organic solid waste pollutant aerobic fermentation system fertilizer.
This method capital equipment is using manual-remote control-adaptivity（USC）Control device, realizes one key of whole system
Start, a key stops operation；On-site manual start and stop, mobile phone or the long-range start and stop of microcomputer and adaptivity (USC) automatic start-stop function,
It can realize unmanned execute-in-place, realize the pollution treatment of organic solid waste pollutant and the fertile multiple spot property formula intelligent management of system.
Polluted in conclusion one group of little module pollution treatment can solve a residential quarters organic waste with fertilizer producing system
Thing；One group of medium module pollution treatment can solve a villages and small towns organic waste pollutant with fertilizer producing system；One group of heavy die block is controlled
It is dirty to solve a small and medium-sized cities organic waste pollutant with fertilizer producing system；Multigroup heavy die block pollution treatment and fertilizer producing system
It can solve the big city organic waste pollutants such as a Shanghai or Beijing.Same reasoning, can tackle all kinds of cultivation
Family organic waste pollutant, field crops organic waste pollutant, municipal sewage plant's organic waste pollutant (wet dirt
Mud), garbage disposal site organic waste pollutant (dewatered sludge).And get twice the result with half the effort for source pollution treatment, implement organic waste pollutant
Do not go out family, do not go out house and do not go out pollution treatment and the fertilizer manufacture of polluted place, be one can undertake the pollution treatment of overall situation high-volume and
The systems technology of system one new concept of fertile task.Harmless treatment is carried out on the day of the organic solid castoff that the same day produces, is solved
Organic solid castoff largely accumulates the global problem of pollution environment.
Brief description of the drawings
Fig. 1 is the pollution treatment of intermittent cyclic tank and the flow sheet of system fertilizer consumption organic solid waste pollutant.
Embodiment
With reference to embodiment, the technical solution in invention is clearly and completely described, described embodiment is only
Only it is the part of the present invention, instead of all the embodiments.
Embodiment one
The pollution treatment of intermittent cyclic tank with system fertilizer consumption residential quarters house refuse organic solid waste pollutant (containing people just and kitchen rubbish
Rubbish, meal Drink rubbish and country fair and each supermarket's rubbish etc.) the step of be：
（1）The organic solid of classification is discarded dirt by Residential Area family, garbage collection points, food and beverage department, country fair and supermarket daily
Contaminate thing and be sent into adaptive type wet-material disintegrator progress pulverization process；Solid water mixture after processing enters three-level solid water with sewage network
Separator carries out separation of solid and liquid, obtains solid material and liquid material.
（2）Liquid material is sent to system sewage-treatment plant and implements sewage disposal.
（3）Solid material is transported in harmless treatment device, implements 70~85 DEG C of high temperature harmless treatments of temperature, time 10
~30 minutes, and the plasma deodorizing apparatus being connected with harmless treatment device is opened, implement waste gas purification deodorization.
（4）After mixed material harmless treatment, continuation of insurance holds 80 DEG C of temperatures above and helps to remove moisture in mixed material, makes it
Water content is 60~65%；When its water content reaches 60~65%, that is, stop heating Bing Qie Change to cool down operation, material to be mixed
When temperature is down to 40~45 DEG C, spraying adds microbial fermentation EM bacterium solutions (inoculation)；Add acidic excipient or basic auxiliary at the same time
PH value is adjusted to more than 6；Carbon/nitrogen auxiliary material adjustment solid material carbon/nitrogen is added than 25~30:1；And continue former, the auxiliary material uniformity and stir
Deodorization operation is mixed and stirred, when the time is about 2~4 small；Realize harmless treatment, modifier treatment, the inoculation of EM bacterium solutions and exhaust air deodorization
Processing.
（5）Through handling and closing symbol technological requirement mixture bacterium material, it is continuous send in solid-state fermentation tank by A periods, B times
Section, C periods aerobic fermentation and the drying of D periods solid material；Reaching curing standard and water content standard can discharge；After discharging
Solid-state fermentation tank on duty by turns can be recycled for non-conservation tank.Degrade within 5 days the decomposed time totally 120 it is small when；1 day non-cutting time is small for 24
When, respectively drying+discharging section totally 18 it is small when；Charging+mixing+harmless treatment+bacterium solution inoculation and deodorization section 2~
4 it is small when；The time cycle of operation is 6 days altogether.System that is to say 5+1 weeks robin, daily using 5 operation+1 non-conservation tanks of tank
The one degraded decomposed time of one non-conservation tank of charging and daily discharging up to 120 it is small when run tank, it is continuous to realize intermittent cyclic tank
Production.System implements system fertilizer using EM microorganism low-temperature bacterium aerobic fermentation process, it is therefore an objective to obtains more, more preferable, more stable
Fertilizer efficiency organic fertilizer and constant temperature energy-saving.
The A periods are the ventilation degraded decomposed period time most fast period, are mixed after mixed material inoculation for microbial bacteria
Material, just starts the decomposed overall process of organic mass degradation in the case where process conditions are manually set；At this time, material body itself aerobic bacteria
Operative temperature edges up up to more than 65 DEG C, and pH value can drop to 5 or so the short time, and the organic substance of microbial bacteria mixed material is fast
Prompt drop solution is decomposed；But the optimal fertilizer efficiency of the organic substance of material in order to control, injects the room temperature wind of 0.2~0.3% amount of mixture volume
(normal temperature air), take away partial material body own temperature and be down to 40~45 DEG C, humidity remain 60~65%, ventilation time is
24 it is small when, obtaining microbial bacteria mixed material, optimal organic substance degrades decomposed fertilizer efficiency and optimal organic substance is degraded decomposed week
Time phase, and it is every 24 it is small when stirring 6~8 times, continue deodorization.
The B periods for ventilation degraded the decomposed period time very fast period, injection microbial bacteria mixture volume 0.1~
The constant temperature wind (40 DEG C are waited warm air) of 0.2% amount, holding temperature is 40~45 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when stirring 4~6 times, continue deodorization.
The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject about 0.1% amount of microbial bacteria mixture volume
Constant temperature wind (40 DEG C wait for warm air), to keep temperature be 40~45 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and often
24 it is small when stirring 2~4 times, continue deodorization.
It is mixed when the decomposed operating mode pH value of the organic matter degradation of microbial bacteria mixed material rises to 7.8~8 in solid-state fermentation tank
Compound material reaches curing standard, can implement the D periods and dry operation, and the 0.2~0.3% of injection microbial bacteria mixture volume
The constant temperature wind (65 DEG C are waited warm air) of amount, and continue stirring dehumidifying, when drying time is about 16 small, reach water content 30%
Discharging.The solid-state fermentation tank is on duty by turns after discharging can be recycled for non-conservation tank.
Embodiment two
The pollution treatment of intermittent cyclic tank and system fertilizer consumption poultry industry raiser's organic solid waste pollutant (containing chicken manure, pig manure, cow dung,
Sheep manure etc.) the step of be：
（1）Feces of livestock and poultry organic solid waste pollutant is sent into house type wet-material disintegrator daily and is crushed by poultry industry raiser
Processing；Solid-liquid Hun He Liao Sui sewage networks after processing enter three-level solid water separator and carry out separation of solid and liquid, obtain solid material
And liquid material.
（2）Liquid material is sent to system sewage-treatment plant and implements sewage disposal.
（3）Solid material+penetrating wind straw obstruct material is delivered into harmless treatment device, implement 70~85 DEG C of high temperature of temperature without
Evilization processing, the time is 10~30 minutes, and opens the plasma deodorizing apparatus being connected with harmless treatment device, and it is net to implement exhaust gas
Eliminate smelly.
（4）After mixed material harmless treatment, continuation of insurance holds 80 DEG C of temperatures above and helps to remove moisture in mixed material, makes it
Water content is 60~65%；When its water content reaches 60~65%, that is, stop heating Bing Qie Change to operation is cooled down, work as mixed material
When temperature is down to 40~45 DEG C, spraying adds microbial fermentation EM bacterium solutions (inoculation)；Add acidic excipient or basic auxiliary at the same time
PH value is adjusted to more than 6；Add ventilative auxiliary material 20%；And continue former, auxiliary material uniformity stirring and deodorization operation, the time is about 2~
4 it is small when, realize harmless treatment, modifier treatment, EM bacterium solutions inoculation and exhaust air deodorization processing.
（5）Through handling and closing symbol technological requirement mixture bacterium material, it is continuous send in solid-state fermentation tank by A periods, B times
Section, C periods aerobic fermentation and the drying of D periods solid material；Solid material aerobic fermentation reaches curing standard and water content standard
It can discharge；Solid-state fermentation tank after discharging is on duty by turns to be can be recycled for non-conservation tank.Degrade within 5 days the decomposed time totally 120 it is small when；1
Its non-cutting time for 24 it is small when, respectively drying+discharging section totally 18 it is small when；Charging+mixing+harmless treatment+bacterium
When liquid is inoculated with and deodorization section 2~4 is small；The time cycle of operation is 6 days altogether.System runs+1 non-conservation tank of tank using 5, namely
5+1 weeks robin, daily the one degraded decomposed time of one non-conservation tank of charging and discharging daily up to 120 it is small when run tank, realize
Intermittent cyclic tank continuous production.System implements system fertilizer using EM microorganism low-temperature bacterium aerobic fermentation process, it is therefore an objective to obtains more
More, more preferable, more stable fertilizer efficiency organic fertilizer and constant temperature energy-saving.
The A periods are the ventilation degraded decomposed period time most fast period, are mixed after mixed material inoculation for microbial bacteria
Material, just starts the decomposed overall process of organic mass degradation in the case where process conditions are manually set；At this time, material body itself aerobic bacteria
Operative temperature edges up up to more than 65 DEG C, and pH value can drop to 5 or so the short time, and the organic substance of microbial bacteria mixed material is fast
Prompt drop solution is decomposed；But the optimal fertilizer efficiency of the organic substance of material in order to control, injects the room temperature wind of 0.2~0.3% amount of mixture volume
(normal temperature air), take away partial material body own temperature and be down to 40~45 DEG C, humidity remain 60~65%, ventilation time is
24 it is small when, obtaining microbial bacteria mixed material, optimal organic substance degrades decomposed fertilizer efficiency and optimal organic substance is degraded decomposed week
Time phase, and it is every 24 it is small when stirring 3~4 times, continue deodorization.
The B periods for ventilation degraded the decomposed period time very fast period, injection microbial bacteria mixture volume 0.1~
The constant temperature wind (40 DEG C are waited warm air) of 0.2% amount, holding temperature is 40~45 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when stirring 2~3 times, continue deodorization.
The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject about 0.1% amount of microbial bacteria mixture volume
Constant temperature wind (40 DEG C wait for warm air), to keep temperature be 40~45 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and often
24 it is small when stirring 1~2 time, continue deodorization.
It is mixed when the decomposed operating mode pH value of the organic matter degradation of microbial bacteria mixed material rises to 7.8~8 in solid-state fermentation tank
Compound material reaches curing standard, can implement the D periods and dry operation, and the 0.2~0.3% of injection microbial bacteria mixture volume
The constant temperature wind (65 DEG C are waited warm air) of amount, and continue stirring dehumidifying, when drying time is about 16 small, reach water content 30%
Discharging.The solid-state fermentation tank is on duty by turns after discharging can be recycled for non-conservation tank.
Embodiment three
The pollution treatment of intermittent cyclic tank consumes agricultural cooperative society's broadacre agriculture organic solid waste pollutant (containing cornstalk, rice with system fertilizer
Bar, straw etc.) the step of be：
（1）Peasant household of agricultural cooperative society, which is daily sent into broadacre agriculture organic solid waste pollutant, temporary to implement three-level and is crushed to
Below 5mm particles obtain solid material and keep in.
（2）Solid material+water is delivered into harmless treatment device, and it is 60%~80% to ensure solid material water content；Implement
70~85 DEG C of high temperature harmless treatments of temperature, time are 10~30 minutes, and connect plasma (or zinc cation+activated carbon is inhaled
Tell) implement waste gas purification deodorization.When its water content reaches 60~65%, spraying adds microbial fermentation YM bacterium solutions (inoculation)；
Acidic excipient is added at the same time or basic auxiliary adjusts pH value to more than 6；Add carbon/nitrogen auxiliary material adjustment solid material carbon/nitrogen than 25~
30:1；80 DEG C of temperatures above are held in continuation of insurance, and continue former, auxiliary material uniformity stirring and deodorization operation, when the time is about 2~4 small,
Realize harmless treatment, modifier treatment and exhaust air deodorization processing.
（3）Through handling and closing symbol technological requirement mixture bacterium material, it is continuous send in solid-state fermentation tank by A periods, B times
Section, C periods aerobic fermentation and the drying of D periods solid material；Solid material aerobic fermentation reaches curing standard and water content standard
It can discharge；Solid-state fermentation tank after discharging is on duty by turns to be can be recycled for non-conservation tank.By microbial bacteria aerobic fermentation process condition
It is required that implement ventilation (air) degraded humus organic material matter；Overall process zinc cation+activated carbon absorption deodorization.Degraded in 5 days is rotten
The ripe time totally 120 it is small when；1 day non-cutting time for 24 it is small when, respectively drying+discharging section totally 18 it is small when；Charging+mixing+
When harmless treatment+bacterium solution inoculation and small deodorization section 2~4；The time cycle of operation is 6 days altogether.System using 5 operation tanks+
1 non-conservation tank, that is to say 5+1 weeks robin, and the one degraded decomposed time of one non-conservation tank of charging and discharging daily is small up to 120 daily
Shi Yunhang tanks, realize intermittent cyclic tank continuous production.System implements system fertilizer using YM microorganism high temperature bacterium aerobic fermentation process,
Purpose is to obtain more optimal organic substance to degrade decomposed fertilizer efficiency and optimal organic substance degraded decomposed period time.
The A periods are the ventilation degraded decomposed period time most fast period, are mixed after mixed material inoculation for microbial bacteria
Material, just starts the decomposed overall process of organic mass degradation in the case where process conditions are manually set；At this time, material body itself aerobic bacteria
Operative temperature edges up up to more than 105 DEG C, and pH value can drop to 5 or so the short time, the organic substance of microbial bacteria mixed material
Fast degradation is decomposed；But the organic substance of material is most preferably degraded decomposed speed in order to control, injects the 0.2~0.3% of mixture volume
The room temperature wind (normal temperature air) of amount, take away partial material body own temperature and be down to 60~65 DEG C, humidity remain 60~65%,
When ventilation time is 24 small, microbial bacteria mixed material is set to obtain the optimal organic substance decomposed fertilizer efficiency of degraded and optimal organic substance
Degrade the decomposed period time, and it is every 24 it is small when stirring 3~4 times, continue deodorization.
The B periods for ventilation degraded the decomposed period time very fast period, injection microbial bacteria mixture volume 0.1~
The constant temperature wind (60 DEG C are waited warm air) of 0.2% amount, holding temperature is 60~65 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when stirring 2~3 times, continue deodorization.
The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject about 0.1% amount of microbial bacteria mixture volume
Constant temperature wind (60 DEG C wait for warm air), to keep temperature be 60~65 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and often
24 it is small when stirring 1~2 time, continue deodorization.
It is mixed when the decomposed operating mode pH value of the organic matter degradation of microbial bacteria mixed material rises to 7.8~8 in solid-state fermentation tank
Compound material reaches curing standard, can implement the D periods and dry operation, and the 0.2~0.3% of injection microbial bacteria mixture volume
The constant temperature wind (65 DEG C are waited warm air) of amount, and continue stirring dehumidifying, when drying time is about 16 small, reach water content 30%
Discharging.The solid-state fermentation tank is on duty by turns after discharging can be recycled for non-conservation tank.
Example IV
The pollution treatment of intermittent cyclic tank with system fertilizer consumption sewage treatment plant's organic solid waste pollutant (wet mud etc.) the step of be：
（1）Sludge organic solid waste pollutant is sent into wet-material disintegrator progress pulverization process daily and obtains standard by sewage treatment plant
Solid material is kept in.
（2）Standard solid material+penetrating wind straw obstruct material+carbon/nitrogen auxiliary material is delivered into harmless treatment device, implements temperature
70~85 DEG C of high temperature harmless treatments are spent, the time is 10~30 minutes, and connects plasma (or zinc cation+activated carbon absorption)
Implement waste gas purification deodorization.When its water content reaches 60~65%, spraying adds microbial fermentation YM bacterium solutions (inoculation)；At the same time
PH value is adjusted to more than 6；80 DEG C of temperatures above are held in continuation of insurance, and continue former, auxiliary material uniformity stirring and deodorization operation, and the time is about
For 2~4 it is small when, realize harmless treatment, modifier treatment and exhaust air deodorization processing.
（3）Through handling and closing symbol technological requirement mixture bacterium material, continuous send will through handling and closing symbol technique to solid-state fermentation tank
Seek mixture bacterium material；It is continuous to send to passing through A periods, B periods, C periods aerobic fermentation and D times in solid aerobic fermentation tank
Section solid material drying；Solid material aerobic fermentation, which reaches curing standard and water content standard, to discharge；Fermentation tank after discharging is
It is reusable.Implement ventilation (air) degraded humus organic material matter by the requirement of microbial bacteria aerobic fermentation process condition；Full mistake
Journey zinc cation+activated carbon absorption deodorization.Degrade within 5 days the decomposed time totally 120 it is small when；When 1 day non-cutting time was 24 small, respectively
For drying+discharging section totally 18 it is small when；When charging+mixing+harmless treatment+bacterium solution inoculation and small deodorization section 2~4；
The time cycle of operation is 6 days altogether.System that is to say 5+1 weeks robin, fed one daily using 5 operation+1 non-conservation tanks of tank
One degraded decomposed time of a non-conservation tank and daily discharging up to 120 it is small when run tank, realize intermittent cyclic tank continuous production.System
System uses YM microorganism high temperature bacterium aerobic fermentation process to implement system fertilizer, it is therefore an objective to obtains the decomposed fertilizer efficiency of more optimal organic substance degraded
Degrade the decomposed period time with optimal organic substance.
The A periods are the ventilation degraded decomposed period time most fast period, are mixed after mixed material inoculation for microbial bacteria
Material, just starts the decomposed overall process of organic mass degradation in the case where process conditions are manually set；At this time, material body itself aerobic bacteria
Operative temperature edges up up to more than 105 DEG C, and pH value can drop to 5 or so the short time, the organic substance of microbial bacteria mixed material
Fast degradation is decomposed；But the organic substance of material is most preferably degraded decomposed speed in order to control, injects the 0.2~0.3% of mixture volume
The room temperature wind (normal temperature air) of amount, take away partial material body own temperature and be down to 60~65 DEG C, humidity remain 60~65%,
When ventilation time is 24 small, microbial bacteria mixed material is set to obtain the optimal organic substance decomposed fertilizer efficiency of degraded and optimal organic substance
Degrade the decomposed period time, and it is every 24 it is small when stirring 3~4 times, continue deodorization.
The B periods for ventilation degraded the decomposed period time very fast period, injection microbial bacteria mixture volume 0.1~
The constant temperature wind (60 DEG C are waited warm air) of 0.2% amount, holding temperature is 60~65 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when stirring 2~3 times, continue deodorization.
The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject about 0.1% amount of microbial bacteria mixture volume
Constant temperature wind (60 DEG C wait for warm air), to keep temperature be 60~65 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and often
24 it is small when stirring 1~2 time, continue deodorization.
It is mixed when the decomposed operating mode pH value of the organic matter degradation of microbial bacteria mixed material rises to 7.8~8 in solid-state fermentation tank
Compound material reaches curing standard, can implement the D periods and dry operation, and the 0.2~0.3% of injection microbial bacteria mixture volume
The constant temperature wind (65 DEG C are waited warm air) of amount, and continue stirring dehumidifying, when drying time is about 16 small, reach water content 30%
Discharging.The solid-state fermentation tank is on duty by turns after discharging can be recycled for non-conservation tank.
Embodiment five
The pollution treatment of intermittent cyclic tank with system fertilizer consumption garbage disposal site organic solid waste pollutant (dewatered sludge etc.) the step of be：
（1）Sludge organic solid waste pollutant is sent into wet-material disintegrator progress pulverization process daily and obtains standard by sewage treatment plant
Solid material is kept in.
（2）Standard solid material is delivered into harmless treatment device, implements 70~85 DEG C of high temperature harmless treatments of temperature, when
Between be 10~30 minutes, and connect plasma (or zinc cation+activated carbon absorption) implement waste gas purification deodorization.When its is aqueous
When amount reaches 60~65%, spraying adds microbial fermentation YM bacterium solutions (inoculation)；Acidic excipient or basic auxiliary adjustment are added at the same time
PH value is to more than 6；Carbon/nitrogen auxiliary material adjustment solid material carbon/nitrogen is added than 25~30:80 DEG C of temperatures above are held in 1 continuation of insurance, and are continued
Former, auxiliary material uniformity stirring and deodorization operation, when the time is about 2~4 small, realize harmless treatment, modifier treatment and exhaust gas
Deodorizing process.
（3）Through handling and closing symbol technological requirement mixture bacterium material, continuous send will through handling and closing symbol technique to solid-state fermentation tank
Seek mixture bacterium material；It is continuous to send to passing through A periods, B periods, C periods aerobic fermentation and D times in solid aerobic fermentation tank
Section solid material drying；Solid material aerobic fermentation, which reaches curing standard and water content standard, to discharge；Fermentation tank after discharging is
It is reusable.Implement ventilation (air) degraded humus organic material matter by the requirement of microbial bacteria aerobic fermentation process condition；Full mistake
Journey zinc cation+activated carbon absorption deodorization.Degrade within 5 days the decomposed time totally 120 it is small when；When 1 day non-cutting time was 24 small, respectively
For drying+discharging section totally 18 it is small when；When charging+mixing+harmless treatment+bacterium solution inoculation and small deodorization section 2~4；
The time cycle of operation is 6 days altogether.System that is to say 5+1 weeks robin, fed one daily using 5 operation+1 non-conservation tanks of tank
One degraded decomposed time of a non-conservation tank and daily discharging up to 120 it is small when run tank, realize intermittent cyclic tank continuous production.System
System uses YM microorganism high temperature bacterium aerobic fermentation process to implement system fertilizer, it is therefore an objective to obtains the decomposed fertilizer efficiency of more optimal organic substance degraded
Degrade the decomposed period time with optimal organic substance.
The A periods are the ventilation degraded decomposed period time most fast period, are mixed after mixed material inoculation for microbial bacteria
Material, just starts the decomposed overall process of organic mass degradation in the case where process conditions are manually set；At this time, material body itself aerobic bacteria
Operative temperature edges up up to more than 105 DEG C, and pH value can drop to 5 or so the short time, the organic substance of microbial bacteria mixed material
Fast degradation is decomposed；But the organic substance of material is most preferably degraded decomposed speed in order to control, injects the 0.2~0.3% of mixture volume
The room temperature wind (normal temperature air) of amount, take away partial material body own temperature and be down to 60~65 DEG C, humidity remain 60~65%,
When ventilation time is 24 small, microbial bacteria mixed material is set to obtain the optimal organic substance decomposed fertilizer efficiency of degraded and optimal organic substance
Degrade the decomposed period time, and it is every 24 it is small when slow stirring 6~8 times, continue deodorization.
The B periods for ventilation degraded the decomposed period time very fast period, injection microbial bacteria mixture volume 0.1~
The constant temperature wind (60 DEG C are waited warm air) of 0.2% amount, holding temperature is 60~65 DEG C, humidity is 55~60%, and ventilation time is small for 48
When, and it is every 24 it is small when slow stirring 4~6 times, continue deodorization.
The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject about 0.1% amount of microbial bacteria mixture volume
Constant temperature wind (60 DEG C wait for warm air), to keep temperature be 60~65 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and often
24 slow stirrings when small 2~4 times, continue deodorization.
When the decomposed operating mode pH value of the organic matter degradation of microbial bacteria mixed material rises to 7.8~8 in solid-state fermentation tank, for up to
To curing standard, can implement the D periods dry operation, the constant temperature of 0.2~0.3% amount of injection microbial bacteria mixture volume
Wind (65 DEG C are waited warm air), and continue stirring dehumidifying, when drying time is about 16 small, reaching water content 30% can discharge.Discharging
The solid-state fermentation tank is on duty by turns afterwards can be recycled for non-conservation tank.
Described above is not limitation of the present invention, and the present invention is also not limited to examples detailed above, the art it is general
Logical technical staff, in the essential scope of the present invention, the variations, modifications, additions or substitutions made, should all belong to the guarantor of the present invention
Protect scope.
Claims (10)
1. a kind of intermittent cyclic tank pollution treatment and the method for system fertilizer consumption organic solid waste pollutant, it is characterised in that：Use
Processing step is as follows：
（1）Daily organic solid waste pollutant to be treated is ground into the solid material of below 5mm sizes；Ensure solid material
Water content is 60%~80%；
（2）Solid material particle delivers into harmless treatment device, and temperature is increased to 70~85 DEG C, is kept for 10~30 minutes, into
Row harmless treatment；And open the emission-control equipment being connected with harmless treatment device and carry out deodorization operation；Harmless treatment
Afterwards, the temperature continuation of insurance in harmless treatment device holds more than 80 DEG C and helps to remove the moisture in solid material；When solid material water content
When being changed into 60~65%, EM bacterium or YM bacterium are added, while it is more than 6 to add acidic excipient or basic auxiliary adjustment solid material pH value,
Carbon/nitrogen auxiliary material adjustment solid material carbon/nitrogen is added than 25~30:1；Continue stirring and deodorization operation, when the time is 2~4 small；
（3）Solid material obtained above is sent to aerobic fermentation is carried out in aerobic fermentation tank, solid material aerobic fermentation reaches curing
Standard and water content standard can discharge, the fermentation tank after discharging, that is, reusable.
2. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：When adding EM bacterium, the temperature of solid material need to be down to 40~45 DEG C could add EM bacterium.
3. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：The additive amount of EM bacterium or YM bacterium is：Solid material per ton adds 1~1.5 kilogram.
4. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：The acidic excipient is one or more of mixing in sulfuric acid, hydrochloric acid and acetic acid；The basic auxiliary is raw
Pulverized limestone.
5. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：The carbon/nitrogen auxiliary material is that the one or more in sugarcane marrow, rice bran, molasses, wheat bran, animal dung and peanut press pulp are mixed
Close.
6. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：When adding EM bacterium, aerobic fermentation need to pass through A periods, B periods, C periods and D periods, and the A periods are
0.2~0.3% 40 DEG C of Tempeerature-constant airs of solid material volume are injected, the temperature of solid material is maintained at 40~45 DEG C, humidity 60
~65%, when ventilation time is 24 small, EM bacterium and solid material is obtained the optimal organic substance decomposed fertilizer efficiency of degraded and optimal organic matter
Matter is degraded the decomposed period time, and it is every 24 it is small when slow stirring 6~8 times；The B periods are very fast for the ventilation degraded decomposed period time
Period, injects 0.1~0.2% 40 DEG C of Tempeerature-constant airs of solid material volume, and it is 40~45 DEG C, humidity to keep solid material temperature
For 55~60%, ventilation time for 48 it is small when, and it is every 24 it is small when slow stirring 4~6 times；The C periods are the decomposed fertilizer efficiency of ventilation degraded
Stabilization time section, injects 0.1% 40 DEG C of Tempeerature-constant airs of solid material volume, holding solid material temperature is 40~45 DEG C, humidity is
50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when slow stirring 2~4 times；The D periods are the organic matter degradation of solid material
When decomposed operating mode pH value rises to 7.8~8, to reach curing standard, can implement the D periods dries operation, injects solid material body
65 DEG C of long-pending 0.2~0.3% wait warm air, and continue stirring dehumidifying, and reaching water content 30% can discharge.
7. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：When adding YM bacterium, aerobic fermentation need to pass through A periods, B periods, C periods and D periods, and the A periods are
60 DEG C of Tempeerature-constant airs of 0.2~0.3% times of amount of solid material volume are injected, the temperature of solid material is maintained at 60~65 DEG C, humidity
Remain 60~65%, ventilation time for 24 it is small when, make YM bacterium and solid material obtain optimal organic substance and degrades decomposed fertilizer efficiency and most
Good organic substance is degraded the decomposed period time, and it is every 24 it is small when stirring 6~8 times；The B periods are the ventilation degraded decomposed period time
The very fast period, injects 0.1~0.2% 60 DEG C of Tempeerature-constant airs of solid material volume, keep solid material temperature for 60~65 DEG C,
Humidity is 55~60%, ventilation time for 48 it is small when, and it is every 24 it is small when stirring 4~6 times；The C periods are the decomposed fertilizer efficiency of ventilation degraded
Stabilization time section, injects 0.1% 60 DEG C of Tempeerature-constant airs of solid material volume, holding solid material temperature is 60~65 DEG C, humidity is
50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when stirring 2~4 times；The D periods are decomposed for the organic matter degradation of solid material
When operating mode pH value rises to 7.8~8, to reach curing standard, can implement the D periods dries operation, injection solid material volume
65 DEG C of 0.2~0.3% wait warm air, and continue stirring dehumidifying, and reaching water content 30% can discharge.
8. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：Solid material can be added with ventilative auxiliary material when delivering into harmless treatment device, and the ventilative auxiliary material is straw
The mixture of one or both of stalk particle and sawdust；Stalk particle is the particle that below 5mm sizes are ground into using stalk；
The additive amount of ventilative auxiliary material accounts for the 20~30% of gross weight；When adding EM bacterium, aerobic fermentation need to pass through A periods, B periods, C
Period and D periods, the A periods are 0.2~0.3% 40 DEG C of Tempeerature-constant airs of injection solid material volume, by solid material
Temperature be maintained at 40~45 DEG C, humidity be 60~65%, ventilation time for 24 it is small when, obtain EM bacterium and solid material optimal organic
The decomposed fertilizer efficiency of mass degradation and optimal organic substance degraded decomposed period time, and it is every 24 it is small when slow stirring 3~4 times；The B times
Section is the ventilation degraded decomposed period time very fast period, injects 0.1~0.2% 40 DEG C of Tempeerature-constant airs of solid material volume, protects
Hold solid material temperature be 40~45 DEG C, humidity be 55~60%, ventilation time for 48 it is small when, and it is every 24 it is small when slow stirring 2~3
It is secondary；The C periods degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject 0.1% 40 DEG C of Tempeerature-constant airs of solid material volume, protect
Hold solid material temperature be 40~45 DEG C, humidity be 50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when slow stirring 1~2
It is secondary；When the D periods rise to 7.8~8 for the decomposed operating mode pH value of organic matter degradation of solid material, to reach curing standard, Bian Keshi
Applying the D periods dries operation, and 65 DEG C of 0.2~0.3% of injection solid material volume wait warm airs, and continue stirring dehumidifying, reach
Water content 30% can discharge.
9. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：Solid material is added with ventilative auxiliary material when delivering into harmless treatment device, the ventilative auxiliary material is broken for stalk
The mixture of grain and one or both of sawdust；Stalk particle is the particle that below 5mm sizes are ground into using stalk；It is ventilative
The additive amount of auxiliary material accounts for the 20~30% of gross weight；When adding YM bacterium, aerobic fermentation need to pass through A periods, B periods, C times
Section and D periods, the A periods are 60 DEG C of Tempeerature-constant airs of 0.2~0.3% times of amount of injection solid material volume, by the temperature of solid material
Degree be maintained at 60~65 DEG C, humidity remain 60~65%, ventilation time for 24 it is small when, make YM bacterium and solid material obtained and most preferably had
The decomposed fertilizer efficiency of machine mass degradation and optimal organic substance degraded decomposed period time, and it is every 24 it is small when stirring 3~4 times；The B periods
Degrade the decomposed period time very fast period for ventilation, inject 0.1~0.2% 60 DEG C of Tempeerature-constant airs of solid material volume, keep
Solid material temperature is 60~65 DEG C, humidity is 55~60%, ventilation time for 48 it is small when, and it is every 24 it is small when stirring 2~3 times；During C
Between section degrade decomposed fertilizer efficiency stabilization time section for ventilation, inject 0.1% 60 DEG C of Tempeerature-constant airs of solid material volume, keep solid
Material temperature degree is 60~65 DEG C, humidity is 50~55%, ventilation time for 48 it is small when, and it is every 24 it is small when stirring 1~2 time；The D periods
When rising to 7.8~8 for the decomposed operating mode pH value of organic matter degradation of solid material, to reach curing standard, can implement the D periods dries
Dry operation, 0.2~0.3% warm airs such as 65 DEG C of injection solid material volume, and continue stirring dehumidifying, reach water content 30% i.e.
It can discharge.
10. intermittent cyclic tank pollution treatment according to claim 1 and the method for system fertilizer consumption organic solid waste pollutant, its
It is characterized in that：The solid material need to carry out separation of solid and liquid when being wet feed, obtain liquid material and water content as 60%~80% solid
Material；Liquid material is transported into sewage-treatment plant and carries out sewage disposal；The solid material need to add water to make solid when being siccative
It is 60%~80% to expect water content.
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| CN108689733A (en) * | 2018-07-20 | 2018-10-23 | 西莱（厦门）生态科技有限公司 | A kind of multistage curing evaporation preparation method of biological organic fertilizer |
| CN110105094A (en) * | 2019-04-10 | 2019-08-09 | 广西大自然再生资源有限公司 | Organic domestic waste biological bacteria fermentation process |
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| CN103964915A (en) * | 2014-06-03 | 2014-08-06 | 天津市农业资源与环境研究所 | Fermentation device for rapidly composting vegetable wastes and using method of fermentation device |
| CN106278487A (en) * | 2016-09-27 | 2017-01-04 | 中国科学院广州能源研究所 | A kind of automatic controlling device utilizing afforestation castoff compost organic and inorganic fertilizer and method |
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| CN110105094A (en) * | 2019-04-10 | 2019-08-09 | 广西大自然再生资源有限公司 | Organic domestic waste biological bacteria fermentation process |
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