CN205999286U

CN205999286U - A kind of organic fertilizer production system

Info

Publication number: CN205999286U
Application number: CN201620981494.0U
Authority: CN
Inventors: 李峰; 杨长煌
Original assignee: Individual
Current assignee: Individual
Priority date: 2016-08-30
Filing date: 2016-08-30
Publication date: 2017-03-08
Anticipated expiration: 2026-08-30

Abstract

The purpose of this utility model is to provide a kind of organic fertilizer production system, including three-level mix selector, slat conveyer and the bucket being sequentially connected with, batch meter, wet solution kettle, discharge bin, disk drying machine, regrading device and pulverizer, the utility model can carry out pipeline to rubbish, and material complete decomposition, stink is little, with short production cycle.

Description

A kind of organic fertilizer production system

Technical field

The utility model belongs to technical field of waste treatment, and in particular to a kind of organic fertilizer production system.

Background technology

With developing rapidly for economic level, domestic city progress faster, urban population occur in that unprecedented swollen Swollen, and requirement more and more higher of the people to quality of the life, resulting a large amount of house refuses, it is flooded with each angle in city Fall, the periphery in city is looped around, the living environment of people is not only damaged, reduce the living standard of people, and pollute environment.With When, a large amount of available resources are there are in these house refuses for going out of use in a large number, for example plastics therein, iron and steel, fiber etc., Most destructor plant has appreciated that the importance of the recycling treatment of house refuse and great economic worth at present, Taking a lot of measures carries out classification process to house refuse, especially the plastics in house refuse, iron and steel, fiber etc. is chosen Out, resource reutilization is carried out, this improves the resource utilization of rubbish to a certain extent.

But the organic matter in house refuse but fails to obtain the utilization of effective scale always, the country is to organic at present The traditional processing mode of thing rubbish is compost treatment, and compost is to concentrate to stack a period of time, warp by the organic matter in house refuse Biochemical degradation is crossed, humus shape is made, the modifying agent as soil or fertilizer.But Traditional compost is generally Anaerobic composting, adopts artificial composting anaerobic composting more, and advantage is that handling process is simple, and in finished product, more preservation nitrogen, has the disadvantage to disappear Organic matter in consumption raw material, composting cycle are oversize, and occupation of land is many, and stink is big, and some materials are not perishable, and germ is difficult to kill, right Environment produces secondary pollution.

Utility model content

The purpose of this utility model is to provide a kind of organic fertilizer production system, can be to the organic matter in house refuse Material carries out pipeline, and material complete decomposition, and stink is little, with short production cycle.

The utility model is adopted the following technical scheme that：

A kind of organic fertilizer production system, including three-level mix selector, slat conveyer and the bucket being sequentially connected with, Batch meter, wet solution kettle, discharge bin, disk drying machine, regrading device and pulverizer, the three-level mix selector is vertically successively It is provided with the first drum sieve, the second drum sieve and the 3rd drum sieve and first drum sieve, the second drum sieve and the 3rd drum sieve Sieve aperture increase successively, the bottom of the first drum sieve is provided with the first discharging opening, and slat conveyer is located at first discharging opening The material that lower section is gone out with delivering sorting is to bucket；

Scale is made up and is provided with to the batch meter of transparent material, and the top of batch meter is by pipeline and the bottom of bucket It is connected and the pipeline between batch meter and bucket is provided with the first valve, the bottom of batch meter is by pipeline and wet solution kettle phase The connection and pipeline between batch meter and wet solution kettle is provided with the second valve, wet solution kettle is provided with for being input into the of high-temperature steam One jet chimney, wet solution kettle is connected with discharge bin by pipeline and the pipeline between wet solution kettle and discharge bin is provided with and spurts Valve；

The top of discharge bin is provided with ejector condenser and discharge bin is provided with the second steaming being connected with ejector condenser Steam pipe road is to export flash-off steam to the ejector condenser；Discharge bin is connected with disk drying machine to convey wet solution Material afterwards is dried process to disk drying machine, and disk drying machine is connected with regrading device to convey drying Material afterwards carries out regrading to regrading device, and regrading device is connected with pulverizer with after feeding secondary screening Material carries out pulverization process to pulverizer.

Further, also include Burning Room, the bottom of the 3rd drum sieve is provided with the 3rd discharging opening and the described 3rd and goes out Material mouth is connected with the Burning Room.

Further, the Burning Room is provided with the 3rd jet chimney and is done with the disc type by the 3rd jet chimney Dry machine is connected, and the vapours produced using Burning Room is carried out the drying of wet solution material, improves heating disk drying machine The utilization rate of rubbish.

Further, the ejector condenser is provided with blow-off pipe, to discharge the sewage produced after steam condensation, makes dirt Water is pooled to sewage treatment plant and carries out concentration purified treatment.

Further, the slat conveyer includes the delivery board being sequentially connected in series, and the both sides of the delivery board are provided with baffle plate, The outer surface of delivery board is coated with rubber layer, the outer surface of delivery board and conveying material directly contact, and coating rubber layer is on the one hand The frictional force between delivery board and material can be increased, be conducive to material is conveyed, another aspect rubber layer corrosion resistance is strong, easily In cleaning, conveying corrosion of the material to delivery board can be effectively prevented, extends the service life of delivery board.

Further, comminutor and blade drier are also included, the comminutor is connected with pulverizer with conveying crushing Material afterwards is granulated to comminutor, obtains organic fertilizer particle, and the blade drier is connected with comminutor to enter The dried process of row organic fertilizer particle, then packs.

The beneficial effects of the utility model are as follows：

The degradable garbage that the utility model is primarily directed in house refuse is processed, so rubbish is passing through this reality Before novel process, artificial separation is carried out first, artificial separation is mainly by larger-size rubbish before mechanical crushing Sort out with the rubbish of some not wettable solutions, mechanical sorting is then carried out, the organic matter of most of wettable solution is separated by mechanical sorting Out, wherein larger-size rubbish is difficult to what wet solution was processed, sends to landfill or burning disposal, and the less rubbish of size leads to Enter high temperature and high pressure steam, react through the wet solution of certain time, so that rubbish is degraded, and so that the material of part degraded is closed again Become humus, emit after the wet solution of rubbish, drying, crush organic fertilizer semi-finished product, then through granulation and Drying process makes organic fertiliser granulates.Specifically, the utility model can form large-scale pipeline formula operation, can carry out The process of a large amount of house refuses, and production procedure can be continuously closed, stink does not expose, and the waste gas of generation, waste water, waste residue all enter Row is processed, and realizes cleanly production, and process cycle is short, and the fertilizer for obtaining has certain economic benefit, realizes rubbish Resource production.

Description of the drawings

Fig. 1 is structural representation of the present utility model；

1st, slat conveyer；2nd, bucket；3rd, batch meter；4th, the first jet chimney；5th, wet solution kettle；6th, discharge bin；7th, spray Penetrate formula condenser；8th, disk drying machine；9th, blow-off pipe；10th, regrading device；11st, pulverizer；12nd, Burning Room；13rd, second Jet chimney；

14th, three-level mix selector；140th, the first drum sieve；141st, the second drum sieve；142nd, the 3rd drum sieve；

15th, the 3rd jet chimney；16th, the first valve；17th, the second valve；18th, blow-off valve；19th, comminutor；20th, paddle is done Dry machine.

Specific embodiment

In order that technical purpose of the present utility model, technical scheme and beneficial effect are clearer, below in conjunction with the accompanying drawings and Specific embodiment is further illustrated to the technical solution of the utility model.

As shown in figure 1, a kind of organic fertilizer production system, including three-level mix selector 14, slat conveyer 1 and sequentially The bucket 2 of connection, wet solution kettle 5, discharge bin 6, disk drying machine 8, regrading device 10 and pulverizer 11, the three-level choosing 14 main body of glassware is the cylindrical drum of a lattice structure, internal diameter 1.8m, and the middle part of cylindrical drum is provided with rotary shaft and rotary shaft drive Cylindrical drum is rotated together, and the end of rotary shaft is provided with motor, 8 ~ 17 revs/min of the rotating speed of rotary shaft, three-level sorting during work 14 right-hand member of device is provided with charging aperture, and cylindrical drum is divided into the first drum sieve 140, the second drum sieve 141 and the 3rd cylinder vertically Sieve 142 and first drum sieve 140, the second drum sieve 141 and the 3rd drum sieve 142 are integrally formed, first drum sieve 140, The sieve aperture of the second drum sieve 141 and the 3rd drum sieve 142 increases successively, the first drum sieve 140, the second drum sieve 141 and the 3rd The screen-aperture size of drum sieve 142 is followed successively by below 50mm, 50 ~ 100mm, more than 100mm, adds from charging aperture so as to material Afterwards, the first drum sieve 140, the second drum sieve 141 and the 3rd drum sieve 142 is passed sequentially through, is carried out point according to material size size Choosing, the bottom of the first drum sieve 140 are provided with the first discharging opening, and inclined upward is arranged slat conveyer 1 to the right, slat conveyer 1 Lower-left end located at the lower section of first discharging opening, the upper right side of slat conveyer 1 located at the top of the bucket 2, from And the material under the first drum sieve 140 is sieved is fallen on slat conveyer 1 by the first discharging opening, the material that then delivering sorting goes out To bucket 2；The slat conveyer 1 includes the delivery board being sequentially connected in series, and the both sides of the delivery board are provided with baffle plate, conveying The outer surface of plate is coated with rubber layer, the outer surface of delivery board and conveying material directly contact；The bottom of the second drum sieve 141 sets Material under having the second discharging opening and sieving carries out landfill disposal, the bottom of the 3rd drum sieve 142 be provided with the 3rd discharging opening and 3rd discharging opening is connected with Burning Room 12, and the material under the sieve of the 3rd drum sieve 142 is delivered to by the 3rd discharging opening and burns Burning in room 12 carries out burning disposal；

Batch meter 3 is provided between the bucket 2 and wet solution kettle 5, quarter is made up and is provided with to the batch meter 3 of transparent material Degree, the top of batch meter 3 be connected with the bottom of bucket 2 by pipeline and the pipeline between batch meter 3 and bucket 2 on set There is the first valve 16, the material fallen in batch meter 3 is controlled by the first valve 16, according to the scale of batch meter 3, when reaching When needing inventory, close the first valve 16, the bottom of batch meter 3 be connected with wet solution kettle 5 by pipeline and batch meter 3 and Pipeline between wet solution kettle 5 is provided with the second valve 17, when the inventory in metering 3 meets demand, opens the second valve 17, Material falls into wet solution kettle 5, and wet solution kettle 5 is provided with the first jet chimney 4 for being input into high temperature and high pressure steam, and the high temperature of input is high Pressure steam carries out wet solution process to the material in wet solution kettle 5, and under hot and humid environment, the material in wet solution kettle 5 is progressively degraded； Wet solution kettle 5 is connected with discharge bin 6 by pipeline and the pipeline between wet solution kettle 5 and discharge bin 6 is provided with blow-off valve 18, degraded After the completion of, the material after degraded is entered in discharge bin 6 by the blow-off valve 18；

The internal design pressure 0.11MPa of discharge bin 6, the material that wet solution is completed are entered low by the wet solution kettle 5 of HTHP In the discharge bin 6 of pressure, there is flash distillation effect in HTHP material, produce a large amount of steams, remove the part moisture in material, release Steam in containing a small amount of pernicious gas, the top of discharge bin 6 is provided with ejector condenser 7 and discharge bin 6 be provided with described The second jet chimney 13 that ejector condenser 7 is connected, the ejector condenser 7 is provided with blow-off pipe 9, in discharge bin 6 Portion produces a large amount of steam due to flash distillation effect, and ejector condenser 7 is sprayed and condenses steam with the water of quantity of steam decades of times, is formed cold Solidifying sewage, the sewage blow-off pipe 9 are flowed in hot sump, and hot sump is delivered to after sewage collecting sewage treatment plant and entered Row concentrates purified treatment.Discharge bin 6 is connected with disk drying machine 8 to convey the material after wet solution to disk drying machine 8 Process is inside dried, and the Burning Room 12 is provided with the 3rd jet chimney 15 and by the 3rd jet chimney 15 and the disk Formula drying machine 8 is connected, disk drying machine 8 by Burning Room 12 material burn produced by high-temperature steam carry out plus Heat, improves the utilization rate of rubbish, and the moisture after dry materials is below 18%；

Disk drying machine 8 is connected to convey dried material to enter to regrading device 10 with regrading device 10 Row regrading, regrading device 10 include screen cloth and the vibrating mechanism that promote screen cloth up-down vibration of the screen-aperture for 20mm, The vibrating mechanism can select box vibrator, and by regrading device 10, the screenings less than 20mm is sized out and enters Next process, is nondegradable such as fragment of brick, cullet etc. thing more than 20mm oversize, directly sends to landfill.Secondary sieve Dividing device 10 to be connected with pulverizer 11 carries out pulverization process with the material after feeding secondary screening to pulverizer 11.This practicality is new Type also includes comminutor 19 and blade drier 20, the comminutor 19 be connected with pulverizer 11 with conveying crushing after material Granulated to comminutor 19, obtained organic fertilizer particle.The blade drier 20 is connected with comminutor phase 19 to carry out The last dried process of organic fertilizer particle, then packs.

To sum up, the utility model obtains available material by house refuse is carried out sorting, then carries out wet solution, drying, powder The broken semi-finished product for obtaining organic fertilizer, then by granulation, dry and are packaged to be organic fertilizer particle.

It should be noted last that：Above-described embodiment is merely to illustrate and unrestricted the technical solution of the utility model, appoints Equivalent and the modification without departing from the utility model spirit and scope or local replacement that what is carried out to the utility model, which is equal Should cover within the utility model protective scope of the claims.

Claims

1. a kind of organic fertilizer production system, it is characterised in that：Including three-level mix selector, slat conveyer and it is sequentially connected with Bucket, batch meter, wet solution kettle, discharge bin, disk drying machine, regrading device and pulverizer, the three-level mix selector Be sequentially provided with vertically the first drum sieve, the second drum sieve and the 3rd drum sieve and first drum sieve, the second drum sieve and The sieve aperture of the 3rd drum sieve increases successively, and the bottom of the first drum sieve is provided with the first discharging opening, and slat conveyer is located at described the The material that the lower section of one discharging opening is gone out with delivering sorting is to bucket；

Scale is made up and is provided with to the batch meter of transparent material, and the top of batch meter is connected with the bottom of bucket by pipeline The logical and pipeline between batch meter and bucket is provided with the first valve, and the bottom of batch meter is connected with wet solution kettle by pipeline And the pipeline between batch meter and wet solution kettle is provided with the second valve, wet solution kettle is provided with the first steaming for being input into high-temperature steam Steam pipe road, wet solution kettle is connected with discharge bin by pipeline and the pipeline between wet solution kettle and discharge bin is provided with blow-off valve；

The top of discharge bin is provided with ejector condenser and discharge bin is provided with the second steam pipe being connected with ejector condenser Road is to export flash-off steam to the ejector condenser.

2. organic fertilizer production system according to claim 1, it is characterised in that：Also include Burning Room, the 3rd circle The bottom of shaft screen is provided with the 3rd discharging opening and the 3rd discharging opening is connected with the Burning Room.

3. organic fertilizer production system according to claim 2, it is characterised in that：The Burning Room is provided with the 3rd steam pipe Road is simultaneously connected with the disk drying machine by the 3rd jet chimney.

4. organic fertilizer production system according to claim 1, it is characterised in that：The ejector condenser is provided with row Dirty pipe.

5. organic fertilizer production system according to claim 1, it is characterised in that：The slat conveyer includes to go here and there successively The delivery board of connection, the both sides of the delivery board are provided with baffle plate, and the outer surface of delivery board is coated with rubber layer.

6. organic fertilizer production system according to claim 1, it is characterised in that：Also include that comminutor and paddle dry Machine, the material after the comminutor is connected with pulverizer with conveying crushing are granulated to comminutor, and the paddle dries Machine is connected with comminutor.