CN213537758U - Complete equipment for preparing fertilizer by treating organic solid waste - Google Patents
Complete equipment for preparing fertilizer by treating organic solid waste Download PDFInfo
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- CN213537758U CN213537758U CN202020375435.5U CN202020375435U CN213537758U CN 213537758 U CN213537758 U CN 213537758U CN 202020375435 U CN202020375435 U CN 202020375435U CN 213537758 U CN213537758 U CN 213537758U
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 27
- 239000002910 solid waste Substances 0.000 title claims abstract description 16
- 230000008878 coupling Effects 0.000 claims abstract description 161
- 238000010168 coupling process Methods 0.000 claims abstract description 161
- 238000005859 coupling reaction Methods 0.000 claims abstract description 161
- 230000007062 hydrolysis Effects 0.000 claims abstract description 60
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 60
- 239000000443 aerosol Substances 0.000 claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000000855 fermentation Methods 0.000 claims abstract description 24
- 230000004151 fermentation Effects 0.000 claims abstract description 24
- 238000004806 packaging method and process Methods 0.000 claims abstract description 8
- 239000000654 additive Substances 0.000 claims description 9
- 230000000996 additive effect Effects 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 58
- 230000018044 dehydration Effects 0.000 abstract description 12
- 238000006297 dehydration reaction Methods 0.000 abstract description 12
- 238000010438 heat treatment Methods 0.000 abstract description 11
- 230000006835 compression Effects 0.000 abstract description 9
- 238000007906 compression Methods 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 9
- 239000003054 catalyst Substances 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 description 13
- 208000005156 Dehydration Diseases 0.000 description 9
- 230000001580 bacterial effect Effects 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 229910010272 inorganic material Inorganic materials 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000010902 straw Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 3
- 230000003116 impacting effect Effects 0.000 description 3
- 238000005381 potential energy Methods 0.000 description 3
- KEQXNNJHMWSZHK-UHFFFAOYSA-L 1,3,2,4$l^{2}-dioxathiaplumbetane 2,2-dioxide Chemical compound [Pb+2].[O-]S([O-])(=O)=O KEQXNNJHMWSZHK-UHFFFAOYSA-L 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 208000027954 Poultry disease Diseases 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
- 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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- Fertilizers (AREA)
Abstract
The utility model discloses a complete set of equipment for processing organic solid wastes to prepare fertilizers, which comprises a coarse crusher, a fine crusher, a hydrolysis tank, a first air heat pump, a second air heat pump, a first reciprocating coupling dehydrator, a second reciprocating coupling dehydrator, a high-pressure draught fan, a gas-water separator, a computer proportioning machine, a fermentation machine, a metering and packaging machine and a control device; the utility model discloses among the hydrolysis process, not add the catalyst or subtract half and add the catalyst, the natural compression heat that air heat pump produced for the material heating pressurization has saved external heating source equipment, accomplishes a tractor serves two-purpose. The dehydration process of the hydrolyzed materials releases aerosol when the compressed heat of an air heat pump is released to normal pressure, the aerosol is mutually coupled in a reciprocating way, one direction of pressurization is released to the other direction of pressurization, the generated aerosol generates impact force to a fixed target at the same time, the two forms of aerosol are released secondarily, the low-temperature dehydration is greatly energy-saving compared with the traditional steam dehydration of the materials which are heated to more than 100 ℃ by a drier, meanwhile, the materials are refined and activated, and the product quality is improved.
Description
Technical Field
The utility model relates to a fertilizer equipment technical field, in particular to constant temperature high pressure hydrolysis and pressurization, the reciprocal coupling of decompression strike the complete sets technical field that produces the novel fertilizer of aerosol dehydration production to fixed target, especially relate to a complete sets of organic solid waste handles system fertilizer.
Background
The organic solid waste refers to human, livestock, poultry excrement, dead bodies of livestock and poultry diseases, kitchen waste after the classification of domestic waste, residual activated sludge of sewage treatment plants, crop straws, forestry waste such as leaves and branches, processed sawdust, waste artificial boards and organic waste after the processing by taking animals and plants as raw materials.
At present, the technologies for preparing the fertilizer by utilizing the organic solid waste mainly comprise the following steps:
1. the conventional organic solid waste hydrolysis fertilizer preparation technology needs to be heated by boiler steam, has the problems of temperature and pressure relevance and poor respective control, and generates volatile organic acid when the temperature exceeds 120 ℃, thereby being the first generation hydrolysis technology. Also has low-temperature pressure hydrolysis with temperature and pressure controlled separately, and can be heated by heat source device alone at temperature not higher than 120 deg.C without producing volatile organic acid. The pressurization uses the higher pressure generated by a piston reciprocating air compressor to supplement the heating temperature of the heating device, and the heating temperature is far lower than 115 ℃ of 120 ℃, so that the heating and the pressurization are separated. Two sets of devices are respectively adopted, which is the second generation hydrolysis technology. Both the first and second generation hydrolysis techniques require the addition of an acidic catalyst.
2. In the first generation and the second generation of hydrolysis technologies, the drier for dehydrating the hydrolyzed wet material has a drier with direct heating and an indirect heating, and the material is dehydrated by water vapor generated by heating the material to more than 150 ℃, so that the energy consumption is high.
3. In order to overcome the defects of the second generation hydrolysis technology, a technology without additionally arranging heat source equipment, namely a normal-temperature high-pressure hydrolysis technology is adopted, and the method is characterized in that no catalyst is added or the catalyst is added in a half amount of 50%. The hydrolysis is carried out without additional heating equipment, so the hydrolysis is called as normal temperature. An air heat pump composed of a piston reciprocating air compressor is used, such as a novel patent 'a novel air heat pump' with patent number 201920182439.9, the air heat pump is used for pressurizing, and the air heat pump naturally compresses heat to generate controllable temperature of 100-200 ℃. The normal temperature is that the hydrolysis material is not required to be heated by a heat source device independently, but is compression heat which is naturally generated in the process of pressurizing by a heat pump and is higher than the ambient temperature, and the machine has two purposes. The high pressure is used for supplementing the deficiency of low temperature, the energy consumption is only the power consumption of a dragging motor of the air heat pump, and the energy is obviously saved compared with the heating by independently arranging a heater.
4. The first generation and the second generation hydrolysis technologies are used for drying and dehydrating wet hydrolysis materials, a drier is used for heating water in the wet hydrolysis materials to be higher than 100 ℃ to form water vapor for dehydration and drying, the temperature of a heat source is higher than 150 ℃, and energy consumption is high.
5. The other steam explosion technology for organic solid waste is one-time puffing by pressurizing and releasing boiler steam, and has no hydrolysis process and no dewatering process of producing normal temperature aerosol by repeatedly pressurizing and releasing pressure to fixed target.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that the existing technology for preparing fertilizer by utilizing organic solid waste is not enough and provides a complete set of equipment for preparing fertilizer by treating organic solid waste, which adopts the air heat pump to pressurize, release pressure and dehydrate in an aerosol form when impacting the generated impact force to a fixed target, and does not form water vapor dehydration in a form. 2 units of pressurizing and pressure releasing devices which are coupled in a reciprocating way are adopted to generate aerosol, the aerosol generated by the reciprocating impact of fixed targets of two opposite devices is conveyed to a gas-water separator by a high-pressure draught fan which generates negative pressure, so that air is separated from water, the air is discharged, and the water is recovered. The hydrolysis technology for dehydrating the normal-temperature aerosol generated by the pressure release and impact on the fixed target is a third generation hydrolysis technology.
The utility model discloses the technical problem that will solve can realize through following technical scheme:
a complete set of equipment for processing organic solid wastes to prepare fertilizers comprises a coarse crusher, a fine crusher, a hydrolysis tank, a first air heat pump, a second air heat pump, a first reciprocating coupling dehydrator, a second reciprocating coupling dehydrator, a high-pressure induced draft fan, a gas-water separator, a computer batching machine, a fermentation machine, a metering and packaging machine and a control device; the discharge hole of the coarse crusher and the discharge hole of the fine crusher are connected with the feed inlet of the hydrolysis tank, the air outlet of the first air heat pump is connected with the air inlet of the hydrolysis tank and the air inlet of the fermentation machine, and the discharge hole of the hydrolysis tank is respectively connected with the total feed inlet of the first reciprocating coupling dehydrator and the total feed inlet of the second reciprocating coupling dehydrator; the circulating feed port of the first reciprocating coupling dehydrator is connected with the circulating discharge port of the second reciprocating coupling dehydrator, and the circulating discharge port of the first reciprocating coupling dehydrator is connected with the circulating feed port of the second reciprocating coupling dehydrator; the total discharge hole of the first reciprocating coupling dehydrator is connected with the first feed inlet of the computer proportioning machine, the total discharge hole of the second reciprocating coupling dehydrator is connected with the second feed inlet of the computer proportioning machine, and the third feed inlet of the computer proportioning machine is connected with the discharge hole of the additive tank; the air outlet of the second air heat pump is respectively connected with the air inlet of the first reciprocating coupling dehydrator and the air inlet of the second reciprocating coupling dehydrator, and the air inlet of the high-pressure induced draft fan is respectively connected with the air outlet of the first reciprocating coupling dehydrator and the air outlet of the second reciprocating coupling dehydrator; an aerosol outlet of the high-pressure induced draft fan is connected with an inlet of the gas-water separator; the feed inlet of the fermentation machine is respectively connected with the discharge outlet of the computer proportioning machine and the discharge outlet of the bacteria liquid tank; the discharge hole of the fermentation machine is connected with the feed inlet of the metering packaging machine; the control device is in control connection with the hydrolysis tank, the first air heat pump, the second air heat pump, the first reciprocating coupling dehydrator and the second reciprocating coupling dehydrator.
In a preferred embodiment of the present invention, the control device is connected to the control of the quick-opening electric discharge valve on the discharge port of the hydrolysis tank; the control device is also respectively in control connection with a motor in the first air heat pump and a motor in the second air heat pump, and is also in signal connection with a pressure sensor in the first air heat pump and a pressure sensor in the second air heat pump; the control device is also respectively connected with the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the gas outlet of the first reciprocating coupling dehydrator and the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the gas outlet of the second reciprocating coupling dehydrator in a control way so as to control the opening states of the control electric valves in the first reciprocating coupling dehydrator and the control electric valves in the second reciprocating coupling dehydrator; meanwhile, the control device is also respectively in signal connection with a time relay in the first reciprocating coupling dehydrator and a time relay in the second reciprocating coupling dehydrator; the control device is also respectively connected with the electric valve and the motor on the air inlet of the high-pressure draught fan in a control mode, and the control device is controlled through programming.
In a preferred embodiment of the present invention, the control device controls the pressure of the hydrolysis tank within a range of 1.0MPa to 4.0MPa, the temperature of the hydrolysis tank is 100 ℃ to 200 ℃ associated with the compression heat generated during the pressurization process of the first air heat pump, and the hydrolysis time of the hydrolysis tank is 2h to 6 h.
In a preferred embodiment of the present invention, the control device controls the pressure of the first reciprocating coupling dehydrator and the second reciprocating coupling dehydrator to be 0.3 MPa-0.8 MPa and the pressurizing time to be 2 min-10 min through the pressure sensor in the second air heat pump, the time relay in the first reciprocating coupling dehydrator, and the time relay in the second reciprocating coupling dehydrator, respectively.
In a preferred embodiment of the present invention, the control device is right for the electric valve switch on the total feed inlet, the circulation discharge outlet, the total discharge outlet, the air inlet, and the air outlet of the first reciprocating coupling dehydrator and the electric valve and the motor on the air inlet of the total feed inlet, the circulation discharge outlet, the total discharge outlet, the air inlet, and the air outlet of the second reciprocating coupling dehydrator, and the control program of the electric valve and the motor on the air inlet of the high pressure draught fan are as follows:
when the first reciprocating coupling dehydrator is pressurized, the motor in the high-pressure induced draft fan is powered off, the electric valve on the air inlet of the high-pressure induced draft fan, the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the air outlet of the first reciprocating coupling dehydrator are all closed, and the control electric valve on the air inlet of the first reciprocating coupling dehydrator and the second air heat pump are opened;
when the first reciprocating coupling dehydrator releases pressure to the second reciprocating coupling dehydrator and impacts a fixed target, an electric valve on an air inlet of a high-pressure induced draft fan, a control electric valve on a circulating discharge hole of the first reciprocating coupling dehydrator, a circulating feed hole of the second reciprocating coupling dehydrator and a control electric valve on an air outlet are all opened, a motor in the high-pressure induced draft fan is electrified and started, a second air heat pump pressurizes the first reciprocating coupling dehydrator and releases pressure to the second reciprocating coupling dehydrator, the second reciprocating coupling dehydrator generates aerosol and impacts the fixed target to generate impact force, and the secondary released aerosol enters a gas-water separator through an aerosol outlet of the high-pressure induced draft fan and an inlet of the gas-water separator to be dehydrated;
on the contrary, when the second reciprocating coupling dehydrator is pressurized, the motor in the high-pressure induced draft fan is powered off, the electric valve on the air inlet of the high-pressure induced draft fan, the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the air outlet of the second reciprocating coupling dehydrator are all closed, and the control electric valve on the air inlet of the second reciprocating coupling dehydrator and the second air heat pump are opened;
when the second reciprocating coupling dehydrator releases pressure to the first reciprocating coupling dehydrator and impacts a fixed target, an electric valve on an air inlet of a high-pressure induced draft fan, a control electric valve on a circulating discharge hole of the second reciprocating coupling dehydrator, a circulating feed hole of the first reciprocating coupling dehydrator and a control electric valve on an air outlet are all opened, a motor in the high-pressure induced draft fan is electrified and started, the second air heat pump pressurizes the second reciprocating coupling dehydrator and releases pressure to the first reciprocating coupling dehydrator, the first reciprocating coupling dehydrator generates aerosol and impacts the fixed target to generate impact force, and the secondary released aerosol enters a gas-water separator through an aerosol outlet of the high-pressure induced draft fan and an inlet of the gas-water separator to be dehydrated;
the first reciprocating coupling dehydrator and the second reciprocating coupling dehydrator are mutually and automatically coupled;
aerosol generated by pressurization, pressure release and impact force to a fixed target enters a gas-water separator through an aerosol outlet of the high-pressure induced draft fan and an inlet of the gas-water separator to separate air and water, the air is emptied, and the water is recycled;
and when the water content of the material reaches 10-30%, the second air heat pump stops pressurizing, releasing pressure and impacting the fixed target.
Compared with the prior art, the utility model has the advantages that:
1. the air pressure generated by the first air heat pump is used for hydrolyzing the organic materials, although the pressure is higher, the compression heat generated by the air heat pump is lower, but no catalyst or half of the catalyst can be added for hydrolyzing the hydrolyzed materials, so that the cost is saved.
2. The first air heat pump is used for pressurizing and simultaneously generating compression heat for hydrolysis, external heat source equipment is not used, the dual purposes of one machine are achieved, and the investment of heat source equipment is saved.
3. And (3) carrying out reciprocating pressurization and pressure release on the first reciprocating coupling dehydrator and the second reciprocating coupling dehydrator by using a second air heat pump to generate aerosol, and simultaneously impacting the aerosol to a fixed target to generate impact force to release the aerosol for the second time, wherein the temperature is normal temperature, the low temperature hydrolysis is about 100 ℃, and the dehydration is not carried out by using a dryer and exceeds 150 ℃ than the dryer. The moisture in the materials is converted into steam for dehydration, and the energy consumption of aerosol dehydration is the electricity consumption cost of a driving motor of the air heat pump. The aerosol generated by the air heat pump is dehydrated by steam of the drier at normal temperature, so that the equipment investment is saved, and the operating cost is reduced.
The utility model discloses a principle is that the electric energy of motor changes mechanical energy into, and the air heat pump that drives piston air compressor machine and constitute changes into compression kinetic energy, changes into the potential energy, and release compression heat resumes the ordinary pressure through the pressure release and absorbs the environment heat, releases the aerosol in the twinkling of an eye through the air drive, and the material obtains popped, refines, the small molecule simultaneously. The kinetic energy is converted into potential energy, so that bound water in the material is converted into aerosol to be released, the activity of the material is increased, and the material is refined and micromolecule-processed. The aerosol is generated by reciprocating pressurization and pressure release, the kinetic energy with strong impact force is generated by impact on a fixed target, the aerosol is generated for secondary dehydration, the organic materials are repeatedly puffed, refined, activated and micromoleculed, the quality of the organic fertilizer is improved, the materials are puffed, refined and micromoleculed by the conversion of physical kinetic energy and potential energy, and the materials are dehydrated in the form of the aerosol instead of dehydrating water vapor in the materials by means of a thermal effect, so that the equipment is simplified, and the machine has two functions.
Drawings
FIG. 1 is a schematic flow diagram of the complete set of equipment for treating organic solid waste to produce fertilizer.
Detailed Description
The invention is further described below with reference to the accompanying drawings and the detailed description.
Organic solid waste includes many types and a wide range. The pretreatment of materials needs coarse crushing and fine crushing, does not need coarse crushing, only needs fine crushing and crushing, only needs to screen impurities, and all kinds of pretreatment process equipment are mature, open and transparent.
Referring to fig. 1, the complete set of equipment for processing organic solid waste to prepare fertilizer shown in the figure comprises a coarse crusher 10, a fine crusher 10, a hydrolysis tank 20, a first air heat pump 30, a second air heat pump 30a, a first reciprocating coupling dehydrator 40, a second reciprocating coupling dehydrator 40a, a high-pressure induced draft fan 50, a gas-water separator 60, a computer dosing machine 70, a fermentation machine 80, a metering and packaging machine 90 and a control device 100.
The coarse and fine crushers 10, the high-pressure draught fan 50, the gas-water separator 60, the computer proportioning machine 70, the fermentation machine 80 and the metering packer 90 are well-known technical equipment and are not described in detail.
The first air heat pump 30 and the second air heat pump 30a are both a new type of air heat pump which has been filed a new patent, patent No. 201920182439.9.
The discharge port 11 of the coarse and fine pulverizer 10 is connected with the feed port 21 of the hydrolysis tank 20, the air outlets 31, 32 of the first air heat pump 30 are connected with the air inlet 22 of the hydrolysis tank 20 and the air inlet 81 of the fermentation machine 80, and the discharge port 23 of the hydrolysis tank 20 is connected with the total feed port 41 of the first reciprocating coupled dehydrator 40 and the total feed port 41a of the second reciprocating coupled dehydrator 40a, respectively.
The circulating feed port 42 of the first reciprocating coupling dehydrator 40 is connected with the circulating discharge port 43a of the second reciprocating coupling dehydrator 40a, and the circulating discharge port 43 of the first reciprocating coupling dehydrator 40 is connected with the circulating feed port 42a of the second reciprocating coupling dehydrator 40 a; the total discharge port 44 of the first reciprocating coupling dehydrator 40 is connected with the first feed port 71 of the computer proportioning machine 70, the total discharge port 44a of the second reciprocating coupling dehydrator 40a is connected with the second feed port 72 of the computer proportioning machine 70, and the third feed port 73 of the computer proportioning machine 70 is connected with the discharge port 111 of the additive tank 110.
The control device 100 is connected with the quick-opening electric discharge valve in the hydrolysis tank 20 in a control way; the control device 100 is also in control connection with the motor in the first air heat pump 30 and the motor in the second air heat pump 30a respectively, and meanwhile, the control device 100 is also in signal connection with the pressure sensor in the first air heat pump 30 and the pressure sensor in the second air heat pump 30 a; the control device 100 is also respectively in control connection with the control electric valve in the first reciprocating coupling dehydrator 40 and the control electric valve in the second reciprocating coupling dehydrator 40a so as to control the opening state of the control electric valve in the first reciprocating coupling dehydrator 40 and the control electric valve in the second reciprocating coupling dehydrator 40 a; meanwhile, the control device 100 is also respectively in signal connection with a time relay in the first reciprocating coupling dehydrator 40 and a time relay in the second reciprocating coupling dehydrator 40 a; the control device 100 is also respectively connected with an electric valve switch and a motor control on the air inlet 51 of the high-pressure draught fan 50, and the control device 100 is controlled by programming.
After crop straws are taken as an example and are crushed into fine materials by a coarse crusher 10 and a fine crusher 10, the materials enter a hydrolysis tank 20 and are supplemented by water because the water content of the straw materials is low and is 15-20 percent. The water adding amount is 1.5 times of the weight of the straws. The air outlet 31 of the first air heat pump 30 is opened to inject air into the air inlet 22 of the hydrolysis tank 20. The pressure in the hydrolysis tank 20 was controlled to 2.5MPa, and the hydrolysis time in the hydrolysis tank 20 was maintained for 4 hours.
When the first air heat pump 30 pressurizes the hydrolysis tank 20 to generate compression heat at 180 ℃ so as to raise the temperature of the material to 100 ℃, controlling the pressure of the hydrolysis tank 20 to be 0.6MPa, opening control electric valves on a main feed port 41 and an air outlet 46 of the first reciprocating coupling dehydrator 40, opening an electric valve and a motor on an air inlet 51 of a high-pressure induced draft fan 50, opening a quick-opening electric discharge valve on a discharge port 23 of the hydrolysis tank 20, so that the material of the hydrolysis tank 20 is sprayed to the first reciprocating coupling dehydrator 40 to release the pressure to the normal pressure, at this time, a large amount of milky aerosol is released from the hydrolysis tank 20, and the sprayed hydrolysis material simultaneously impacts a fixed target on the upper part of the first reciprocating coupling dehydrator 40 to generate impact force, the milky aerosol in the material is released for the second time, and the aerosol released for the second time is sent to the gas-water separator 60 by the negative pressure of the high-pressure induced draft, air is discharged and water is recovered.
The degassed sol mass of the first reciprocating coupling dehydrator 40 sinks to the lower portion. The control electric valves of the main feed inlet 41, the circulation feed inlet 42, the circulation discharge outlet 43, the main discharge outlet 44 and the air outlet 46 of the first reciprocating coupling dehydrator 40, the electric valve and the motor on the air inlet 51 of the high-pressure induced draft fan 50 are turned off, the control electric valve on the air inlet 45 of the first reciprocating coupling dehydrator 40 is turned on at the same time, compressed air is injected into the first reciprocating coupling dehydrator 40 from the air outlet 31a of the second air heat pump 30a and the air inlet 45 of the first reciprocating coupling dehydrator 40, the pressure sensor in the first reciprocating coupling dehydrator 40 is controlled by the control device 100, and the pressure is kept for 2min when the pressure is controlled to be 0.6 MPa.
Then opening a control electric valve on a circulation discharge port 43 of the first reciprocating coupling dehydrator 40, a control electric valve on a circulation feed port 42a of the second reciprocating coupling dehydrator 40a, a control electric valve on an air outlet 46a of the second reciprocating coupling dehydrator 40a and an electric valve on an air inlet 51 of a high-pressure induced draft fan 50, rapidly discharging the first reciprocating coupling dehydrator 40, releasing pressure to shoot into the second reciprocating coupling dehydrator 40a to immediately generate milky aerosol, and simultaneously enabling the high-speed sprayed material to flow to a fixed target of the second reciprocating coupling dehydrator 40a to impact, so that the aerosol in the hydrolyzed material is released secondarily due to strong impact force.
The aerosol released twice is automatically input into the gas-water separator 60 for air and water separation by the negative pressure generated by the high-pressure induced draft fan 50 at the upper part of the second reciprocating coupling dehydrator 40a, and the air is discharged and the water is recovered.
The hydrolyzed material in the second reciprocating coupling dehydrator 40a falls into the lower part, the control electric valves of the main feed inlet 41a, the circulating feed inlet 42a, the circulating discharge outlet 43a, the main discharge outlet 44a and the air outlet 46a of the second reciprocating coupling dehydrator 40a, the electric valve and the motor on the air inlet 51 of the high-pressure induced draft fan 50 are closed, the control electric valve on the air inlet 45a of the second reciprocating coupling dehydrator 40a is opened, the compressed air is injected into the second reciprocating coupling dehydrator 40a from the air outlet 31a of the second air heat pump 30a and the air inlet 45a of the second reciprocating coupling dehydrator 40a, the pressure sensor in the second reciprocating coupling dehydrator 40a is controlled by the control device 100, and the pressure is maintained for 2min when the pressure is controlled to be 0.6 MPa.
Then opening a control electric valve on a circulating discharge hole 43a of the second reciprocating coupling dehydrator 40a, a control electric valve on a circulating feed hole 42 of the first reciprocating coupling dehydrator 40, a control electric valve on an air outlet 46 of the first reciprocating coupling dehydrator 40, and an electric valve on an air inlet 51 of a high-pressure induced draft fan 50, and rapidly discharging the second reciprocating coupling dehydrator 40a, releasing pressure and ejecting the pressure to the first reciprocating coupling dehydrator 40 to immediately generate milk-white aerosol, and simultaneously ejecting material flow at high speed to impact a fixed target of the first reciprocating coupling dehydrator 40, so that the aerosol in the hydrolyzed material is released secondarily by strong impact force. The aerosol released twice is automatically input into the gas-water separator 60 for air and water separation by the negative pressure generated by the high-pressure induced draft fan 50 at the upper part of the first reciprocating coupling dehydrator 40, and the air is discharged and the water is recovered.
The first reciprocating coupling dehydrator 40 and the second reciprocating coupling dehydrator 40a are used for mutual pressurization and pressure release, impact is carried out on a fixed target, and aerosol is released for dehydration for the second time, wherein the reciprocating times are reciprocating for 4 times based on the water content of the material reaching 20%. The water content of the material reaches 19.4 percent. The dehydrated dry materials are loosened to obtain the mixed materials with the fineness of 60 meshes to 80 meshes.
After the mixed material meets the requirement, the electric control valve on the total discharge hole 44 of the first reciprocating coupling dehydrator 40 or the electric control valve on the total discharge hole 44a of the second reciprocating coupling dehydrator 40a is opened to discharge, and the mixed material is conveyed to the computer proportioning machine 70 by the conveyor.
If producing organic-inorganic compound fertilizer, the fertilizer additive is added to the computer proportioning machine 70 through the additive tank 110 for proportioning to obtain the organic-inorganic compound fertilizer.
If the compound microorganism mixing material is produced, the computer dosing machine 70 conveys the mixed material added with the fertilizer additive into the fermentation machine 80, simultaneously, the bacterial liquid in the bacterial liquid groove 120 is also added into the fermentation machine 80 for fermentation, after the fermentation is mature and the number of the beneficial viable bacteria reaches the standard, the air of the first air heat pump 30 is injected into the fermentation machine 80 to be forcedly dehydrated to the standard of less than or equal to 30 percent, and finally, the metering, packaging and the product is stored in a warehouse.
Or:
when the first air heat pump 30 pressurizes the hydrolysis tank 20 to generate compression heat at 180 ℃ so as to raise the temperature of the material to 100 ℃, controlling the pressure of the hydrolysis tank 20 to be 0.6MPa, opening control electric valves on a main feed inlet 41a and an air outlet 46a of the second reciprocating coupling dehydrator 40a, opening an electric valve and a motor on an air inlet 51a of a high-pressure induced draft fan 50a, opening a quick-opening electric discharge valve on a discharge outlet 23 of the hydrolysis tank 20, and spraying and releasing the pressure of the material in the hydrolysis tank 20 to the second reciprocating coupling dehydrator 40a to normal pressure, at this time, a large amount of milky aerosol is released from the hydrolysis tank 20, and simultaneously the sprayed hydrolysis material impacts a fixed target on the upper part of the second reciprocating coupling dehydrator 40a to generate impact force, and secondly release the milky aerosol in the material, and the secondly released aerosol is sent to the gas-water separator 60 by the negative pressure of the high-pressure induced draft fan 50 to separate air and water, air is discharged and water is recovered.
The degassed sol mass of the second reciprocating coupling dehydrator 40a sinks to the lower portion. The control electric valves of the main feed inlet 41a, the circulation feed inlet 42a, the circulation discharge outlet 43a, the main discharge outlet 44a and the air outlet 46a of the second reciprocating coupling dehydrator 40a, and the electric valve and the motor on the air inlet 51 of the high-pressure induced draft fan 50 are turned off, the control electric valve on the air inlet 45a of the second reciprocating coupling dehydrator 40a is turned on, compressed air is injected into the second reciprocating coupling dehydrator 40a from the air outlet 31a of the second air heat pump 30a and the air inlet 45a of the second reciprocating coupling dehydrator 40a, the pressure sensor in the second reciprocating coupling dehydrator 40a is controlled by the control device 100, and the pressure is continuously maintained for 2min when the pressure is controlled to be 0.6 MPa.
Then opening a control electric valve on a circulating discharge hole 43a of the second reciprocating coupling dehydrator 40a, a control electric valve on a circulating feed hole 42 of the first reciprocating coupling dehydrator 40, a control electric valve on an air outlet 46 of the first reciprocating coupling dehydrator 40, and an electric valve on an air inlet 51 of a high-pressure induced draft fan 50, and rapidly discharging the second reciprocating coupling dehydrator 40a, releasing pressure and ejecting the pressure to the first reciprocating coupling dehydrator 40 to immediately generate milk-white aerosol, and simultaneously ejecting material flow at high speed to impact a fixed target of the first reciprocating coupling dehydrator 40, so that the aerosol in the hydrolyzed material is released secondarily by strong impact force.
The aerosol released twice is automatically input into the gas-water separator 60 for air and water separation by the negative pressure generated by the high-pressure induced draft fan 50 at the upper part of the first reciprocating coupling dehydrator 40, and the air is discharged and the water is recovered.
The hydrolyzed material in the first reciprocating coupling dehydrator 40 falls into the lower part, the control electric valves of the main feed inlet 41, the circulating feed inlet 42, the circulating discharge outlet 43, the main discharge outlet 44 and the air outlet 46 of the first reciprocating coupling dehydrator 40, the electric valve and the motor on the air inlet 51 of the high-pressure induced draft fan 50 are closed, the control electric valve on the air inlet 45 of the first reciprocating coupling dehydrator 40 is opened at the same time, compressed air is injected into the first reciprocating coupling dehydrator 40 from the air outlet 31a of the second air heat pump 30a and the air inlet 45 of the first reciprocating coupling dehydrator 40, the pressure sensor in the first reciprocating coupling dehydrator 40 is controlled by the control device 100, and the pressure is kept for 2min when the pressure is controlled to be 0.6 MPa.
Then opening a control electric valve on a circulation discharge port 43 of the first reciprocating coupling dehydrator 40, a control electric valve on a circulation feed port 42a of the second reciprocating coupling dehydrator 40a, a control electric valve on an air outlet 46a of the second reciprocating coupling dehydrator 40a and an electric valve on an air inlet 51 of a high-pressure induced draft fan 50, rapidly discharging the first reciprocating coupling dehydrator 40, releasing pressure to shoot into the second reciprocating coupling dehydrator 40a to immediately generate milky aerosol, and simultaneously enabling the high-speed sprayed material to flow to a fixed target of the second reciprocating coupling dehydrator 40a to impact, so that the aerosol in the hydrolyzed material is secondarily released due to strong impact force. The aerosol released twice is automatically input into the gas-water separator 60 for air and water separation by the negative pressure generated by the high-pressure induced draft fan 50 at the upper part of the second reciprocating coupling dehydrator 40a, and the air is discharged and the water is recovered.
The second reciprocating coupling dehydrator 40a and the first reciprocating coupling dehydrator 40 mutually pressurize and release pressure, impact on the fixed target, release aerosol for dehydration for the second time, and the reciprocating times are reciprocating for 4 times based on the water content of the material reaching 20%. The water content of the material reaches 19.4 percent. The dehydrated dry materials are loosened to obtain the mixed materials with the fineness of 60 meshes to 80 meshes.
After the mixed material meets the requirement, the electric control valve on the total discharge hole 44 of the first reciprocating coupling dehydrator 40 or the electric control valve on the total discharge hole 44a of the second reciprocating coupling dehydrator 40a is opened to discharge, and the mixed material is conveyed to the computer proportioning machine 70 by the conveyor.
If producing organic-inorganic compound fertilizer, the fertilizer additive is added to the computer proportioning machine 70 through the additive tank 110 for proportioning to obtain the organic-inorganic compound fertilizer.
If the compound microorganism mixing material is produced, the computer dosing machine 70 conveys the mixed material added with the fertilizer additive into the fermentation machine 80, simultaneously, the bacterial liquid in the bacterial liquid groove 120 is also added into the fermentation machine 80 for fermentation, after the fermentation is mature and the number of the beneficial viable bacteria reaches the standard, the air of the first air heat pump 30 is injected into the fermentation machine 80 to be forcedly dehydrated to the standard of less than or equal to 30 percent, and finally, the metering, packaging and the product is stored in a warehouse.
The complete equipment of the utility model can produce various organic fertilizers, including common organic fertilizers, biological organic fertilizers, compound microbial fertilizers, agricultural microbial agents and the like.
Although an embodiment of the present invention has been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to this embodiment without departing from the principles and spirit of the invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (2)
1. A complete set of equipment for processing organic solid wastes to prepare fertilizers is characterized by comprising a coarse crusher, a fine crusher, a hydrolysis tank, a first air heat pump, a second air heat pump, a first reciprocating coupling dehydrator, a second reciprocating coupling dehydrator, a high-pressure induced draft fan, a gas-water separator, a computer proportioning machine, a fermentation machine, a metering and packaging machine and a control device; the discharge hole of the coarse crusher and the discharge hole of the fine crusher are connected with the feed inlet of the hydrolysis tank, the air outlet of the first air heat pump is connected with the air inlet of the hydrolysis tank and the air inlet of the fermentation machine, and the discharge hole of the hydrolysis tank is respectively connected with the total feed inlet of the first reciprocating coupling dehydrator and the total feed inlet of the second reciprocating coupling dehydrator; the circulating feed port of the first reciprocating coupling dehydrator is connected with the circulating discharge port of the second reciprocating coupling dehydrator, and the circulating discharge port of the first reciprocating coupling dehydrator is connected with the circulating feed port of the second reciprocating coupling dehydrator; the total discharge hole of the first reciprocating coupling dehydrator is connected with the first feed inlet of the computer proportioning machine, the total discharge hole of the second reciprocating coupling dehydrator is connected with the second feed inlet of the computer proportioning machine, and the third feed inlet of the computer proportioning machine is connected with the discharge hole of the additive tank; the air outlet of the second air heat pump is respectively connected with the air inlet of the first reciprocating coupling dehydrator and the air inlet of the second reciprocating coupling dehydrator, and the air inlet of the high-pressure induced draft fan is respectively connected with the air outlet of the first reciprocating coupling dehydrator and the air outlet of the second reciprocating coupling dehydrator; an aerosol outlet of the high-pressure induced draft fan is connected with an inlet of the gas-water separator; the feed inlet of the fermentation machine is respectively connected with the discharge outlet of the computer proportioning machine and the discharge outlet of the bacteria liquid tank; the discharge hole of the fermentation machine is connected with the feed inlet of the metering packaging machine; the control device is in control connection with the hydrolysis tank, the first air heat pump, the second air heat pump, the first reciprocating coupling dehydrator and the second reciprocating coupling dehydrator.
2. The plant for producing fertilizer by treating organic solid waste as claimed in claim 1, wherein the control device is connected with a quick-opening electric discharge valve control on the discharge port of the hydrolysis tank; the control device is also respectively in control connection with a motor in the first air heat pump and a motor in the second air heat pump, and is also in signal connection with a pressure sensor in the first air heat pump and a pressure sensor in the second air heat pump; the control device is also respectively connected with the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the gas outlet of the first reciprocating coupling dehydrator and the control electric valves on the main feed inlet, the circulating discharge outlet, the main discharge outlet and the gas outlet of the second reciprocating coupling dehydrator in a control way so as to control the opening states of the control electric valves in the first reciprocating coupling dehydrator and the control electric valves in the second reciprocating coupling dehydrator; meanwhile, the control device is also respectively in signal connection with a time relay in the first reciprocating coupling dehydrator and a time relay in the second reciprocating coupling dehydrator; the control device is also respectively connected with the electric valve and the motor on the air inlet of the high-pressure draught fan in a control mode, and the control device is controlled through programming.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111423260A (en) * | 2020-03-23 | 2020-07-17 | 刘文治 | Complete equipment for preparing fertilizer by treating organic solid waste |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111423260A (en) * | 2020-03-23 | 2020-07-17 | 刘文治 | Complete equipment for preparing fertilizer by treating organic solid waste |
| CN111423260B (en) * | 2020-03-23 | 2024-05-14 | 刘文治 | Complete equipment for preparing fertilizer by organic solid waste treatment |
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