CN201367400Y - Multi-compartment organic fertilizer processing device - Google Patents

Abstract

The utility model relates to a multi-compartment organic fertilizer processing device, which comprises a plurality of processing units, at least one heater, a preheating unit, a return water unit, a cooling unit and a heat source unit. Each processing unit includes a reaction compartment and a coil pipe, wherein the reaction compartment is used for placing organic fertilizers and the coil pipe is arranged in the reaction compartment. Through the return water unit, the water flowing through the coil pipe is collected. Moreover, after the water is heated by the heater, the water circularly flows into the coil pipe. Thereby, through the method of circulation, the heat generated during temperature reduction of each reaction compartment is recycled and the heat consumed during water heating is reduced.

Description

Multi-channel organic fertilizer treatment unit

Technical field

The utility model relates to a kind of organic fertilizer treatment unit, refers in particular to a kind of multi-channel organic fertilizer treatment unit.

Background technology

Usually conduct livestock waste and sewage sludge etc. contain the moisture organic waste, and when further making organic fertilizer by organic waste, usually after this organic waste and drying material being dropped into the room of a hollow cylinder, turn round this cylindrical shell, organic waste, drying material and microorganism are mixed, and this mixture fermented with the condition of high temperature, after maturation, make organic fertilizer again.

Consult Fig. 1, be No. 219857 " full-automatic organic fertilizer generates machine " utility model patent of TaiWan, China, the cylinder 11, one that this organic fertilizer generates facility and have an arranged transversely drives CD-ROM drive motor 12, that this cylinder 11 rotates and is located at the drawing mechanism 14 that the feeding device 13, of the inlet end of this cylinder 11 is located at the exit end of this cylinder 11, and a heating tube 15 of being located at the shaft core position of these cylinder 11 inside.

Utilize above-mentioned design, organic fertilizer is sent in this cylinder 11 from this feeding device 13, this CD-ROM drive motor 12 can drive this cylinder 11 and rotate, in order to stir organic fertilizer wherein, and utilize the hot gas that this heating tube 15 blows out that the organic fertilizer in this cylinder 11 are heated, treat that afterwards this cylinder 11 leaves standstill and makes organic fertilizer cooling and fermentation wherein and finishes the maturation of organic fertilizer.

Yet, because generating machine, this organic fertilizer only has single cylinder 11,11 spaces that can take up ccontaining fertilizer of this cylinder are limited, adding organic fertilizer need pass through steps such as heating, cooling and fermentation and just be able to maturation, therefore, the organic fertilizer that every echelon is produced is not only consuming time but also output is limited, so can't make a large amount of organic fertilizer at short notice, and repeatedly repeat heating and the cooling carried out at this cylinder 11, the consumption that improves its heating energy source relatively.

Moreover, because this cylinder 11 is closed, only the inlet end with pan feeding communicates with the external world with the exit end of discharging, after the organic fertilizer of this cylinder 11 carries out heat treated, be merely able to dispel the heat, therefore, will cause the organic fertilizer in this cylinder 11 to be difficult for cooling by inlet end and exit end, cause organic fertilizer long required cooling time, and then influence the operating efficiency that this organic fertilizer generation machine is handled organic fertilizer.

The utility model content

The purpose of this utility model provides a kind of multi-channel organic fertilizer treatment unit of saving the energy and improving operating efficiency and output.

Multi-channel organic fertilizer treatment unit described in the utility model, comprise that backwater unit, that preheating unit, that a plurality of processing units, at least one well heater, that water liquid heating back is flowed into described processing unit are equipped with water liquid stores water liquid is equipped with the cooling unit of water liquid, and a heat source unit.

Each is handled unit pack and draws together one for the ccontaining reactive tank of organic fertilizer, reach a coil pipe that is arranged in this reactive tank, this well heater can flow into water liquid heating back in the coil pipe of described processing unit, and this preheating unit comprises that one is equipped with the preheated tank of water liquid, and is placed in the coil pipe that the interior water liquid of this preheated tank can flow into described processing unit through this well heater.

This backwater unit comprises that one stores the recovery tank of the effusive water liquid of coil pipe, and the water liquid in this recovery tank can flow into via this well heater in the coil pipe of described processing unit again and form circulation.

This cooling unit comprises a ccontaining water liquid and is communicated with the cooling tank of described coil pipe that the water liquid in this cooling tank can flow in the coil pipe of described processing unit, and the effusive water liquid of the coil pipe of described processing unit can be concentrated and the formation circulation toward this cooling tank again.This heat source unit is to be communicated with this cooling tank and this preheated tank and to heat the water liquid in the preheated tank and the water liquid in the cooling tank of this cooling unit carried out heat exchange.

Multi-channel organic fertilizer treatment unit described in the utility model, this backwater unit comprises that also one is communicated with the pipe connecting of this recovery tank and this preheated tank, the backwater rising pipe of a plurality of these recovery tanks of connection, a plurality of backwater outlet valves that are arranged on the corresponding backwater rising pipe, the backwater water inlet pipe of a plurality of these recovery tanks of connection, and a plurality of backwater water intaking valves that are arranged on the corresponding backwater water inlet pipe, each backwater rising pipe is communicated with corresponding coil pipe with each backwater water inlet pipe, and this multi-channel organic fertilizer treatment unit comprises a plurality of these well heaters that are located on the corresponding backwater rising pipe that connect.

Multi-channel organic fertilizer treatment unit described in the utility model, each processing unit also comprises the dividing plate of the bottom of being located at this reactive tank, each handles the warming chamber that defines a ccontaining water liquid between unitary dividing plate and the reactive tank, and described warming chamber and this preheated tank are interconnected.

Multi-channel organic fertilizer treatment unit described in the utility model, this cooling unit also comprises the cooling rising pipe of a plurality of these cooling tanks of connection, a plurality of cooling outlet valve on the corresponding cooling rising pipe, cooling water inlet pipe of a plurality of these cooling tanks of connection of being arranged on, and a plurality of cooling water intaking valves that are arranged on the corresponding cooling water inlet pipe.

Multi-channel organic fertilizer treatment unit described in the utility model, this heat source unit comprises a Heat source device that is communicated with this preheated tank and the water liquid in this preheated tank can be heated, reach one and be communicated with this preheated tank and this cooling tank, the water source unit that carries out heat exchange with water liquid the water liquid in the cooling tank and this preheated tank.

Multi-channel organic fertilizer treatment unit described in the utility model, this water source unit have that vaporizer, that expansion valve, that the first-class condenser that is connected with cold medium, is communicated with this condenser is communicated with this expansion valve is communicated with that this condenser and the compressor, of this vaporizer are located on this vaporizer and can with the intensification pipeline of cold medium heat exchange in this vaporizer, reach one be located on this condenser and can with the cooling pipeline of the cold coal heat exchange of this condenser.

Multi-channel organic fertilizer treatment unit described in the utility model, each well heater has a tubular body, and is arranged at the inner ring surface of this tubular body and is arranged at the inner ring surface of this tubular body and second electric-conductor that is connected with the negative electricity of this power supply with first electric-conductor, that the positive pole of a power supply is electrically connected at intervals with this first electric-conductor, reaches two earthings that link to each other with this tubular body respectively and is arranged at the separator of two end opposite of this tubular body.

Multi-channel organic fertilizer treatment unit described in the utility model, each processing unit comprise that also one is arranged in this reactive tank in order to stir the agitator of organic fertilizer.

The beneficial effects of the utility model are: by the unitary recovery tank of this backwater, stream is concentrated by the water liquid of described coil pipe, and circulate once more after utilizing this well heater with the heating of water liquid and flow in the described coil pipe, not only recycle the heat after each reactive tank cooling, reduce the heat energy that is consumed when water liquid heats, can also improve the output and the operating efficiency of organic fertilizer.

Description of drawings

Fig. 1 is a side-view, illustrates that the full-automatic organic fertilizer of No. the 219857th, TaiWan, China generates machine.

Fig. 2 is a synoptic diagram, and the preferred embodiment of the utility model multi-channel organic fertilizer treatment unit is described.

Fig. 3 is a part of sectional view, and the aspect of the well heater of this preferred embodiment is described.

Fig. 4 is a part of synoptic diagram, and the aspect of the water source unit of this preferred embodiment is described.

Fig. 5 is a part of synoptic diagram, and the aspect of the heating pipelining of this preferred embodiment is described.

Fig. 6 is a part of synoptic diagram, and the aspect of the cooling pipelining of this preferred embodiment is described.

Embodiment

Below in conjunction with drawings and Examples the utility model is elaborated.

Consult Fig. 2, the preferred embodiment of the utility model multi-channel organic fertilizer treatment unit comprises three processing units 2, three well heaters 3, a preheating unit 4, a backwater unit 5, a cooling unit 6 and heat source units 7.

Each processing unit 2 comprises that one is arranged in this reactive tank 21 and is surrounded on the coil pipe 22 of cell wall for organic fertilizer ccontaining reactive tank 21,, and one be located at these reactive tank 21 bottoms and be skewed dividing plate 23, and be arranged in this reactive tank 21 in order to stir the agitators 24 of organic fertilizer, define a ccontaining water liquid between the dividing plate 23 of each processing unit 2 and the reactive tank 21 and be awl cyclic warming chamber 25, and when this reactive tank 21 of sealing, can make the inside and the extraneous thermal isolation of this reactive tank 21.

This preheating unit 4 comprise one can ccontaining water liquid preheated tank 41, this preheated tank 41 is interconnected with the warming chamber 25 of described processing unit 2, and this preheated tank 41 can open and close the tap water that control flows into by a gate 44 at any time, makes these preheated tank 41 interior water liquid maintain the water liquid capacity of setting.

This backwater unit 5 comprises that one stores the recovery tank 51 of water liquid, one is communicated with the pipe connecting 52 of the preheated tank 41 of this recovery tank 51 and this preheating unit 4, the backwater rising pipe 53 of this recovery tank 51 of a plurality of connections, a plurality of backwater outlet valves 54 that are arranged on the corresponding backwater rising pipe 53, the backwater water inlet pipe 55 of this recovery tank 51 of a plurality of connections, and a plurality of backwater water intaking valves 56 that are arranged on the corresponding backwater water inlet pipe 55, and this preheating unit 4 also has the connection valve of being located on this pipe connecting 52 43, in order to open and close the water liquid of these preheated tank 41 these recovery tanks 51 of inflow of control, in addition, this recovery tank 51 reclaims the water liquid after described coil pipe 22 heat exchanges, and then the water liquid that makes this recovery tank 51 can maintain 75 ℃～90 ℃, water liquid in this preheated tank 41 can flow in this recovery tank 51 through this pipe connecting 52, flows into the coil pipe 22 of described processing unit 2 again via described backwater rising pipe 53 and well heater 3.

Each backwater rising pipe 53 is communicated with the coil pipe 22 of corresponding processing unit 2 with each backwater water inlet pipe 55, the coil pipe 22 effusive water liquid of described processing unit 2 can be concentrated toward this recovery tank 51 through each backwater water inlet pipe 55, afterwards, water liquid is flowed out by each backwater rising pipe 53 and in the corresponding well heater 3 of flowing through again, then, flow into again in the coil pipe 22 of described processing unit 2 and form circulation, described well heater 3 connects and is located on the corresponding backwater rising pipe 53, and can the water liquid in the described backwater rising pipe 53 be flowed in the coil pipe 22 of described processing unit 2 again with after the water liquid heating in the described backwater rising pipe 53.

Consult Fig. 2, Fig. 3, each well heater 3 has the tubular body 31 of the corresponding backwater rising pipe 53 of a connection, one first electric-conductor 32 that is arranged at these tubular body 31 inner ring surfaces and is electrically connected with the positive pole 301 of a power supply 30, one second electric-conductor 33 that is arranged at these tubular body 31 inner ring surfaces at intervals and is electrically connected with this first electric-conductor 32 with the negative pole 302 of this power supply 30, two earthings that link to each other with this tubular body 31 respectively are arranged at first separator 34 and second separator 35 of 31 liang of end opposite of this tubular body, this first electric-conductor 32 and second electric-conductor 33 are only by water liquid conducting in this tubular body 31 and generation one electric field with matching, and then the water liquid that circulates in is wherein heated, and this first separator 34, second separator 35 can be derived the electric current in the water liquid, avoids electric current to flow out the situation that this well heater 3 causes electric leakage outward.

This cooling unit 6 comprise one can ccontaining water liquid cooling tank 61, the cooling rising pipe 62 of this cooling tank 61 of a plurality of connection, a plurality of cooling water inlet pipe 64 that is arranged on the cooling outlet valve 63 on the corresponding cooling rising pipe 62, this cooling tank 61 of a plurality of connection, and a plurality of cooling water intaking valves 65 that are arranged on the corresponding cooling water inlet pipe 64.

Water liquid in this cooling tank 61 can cool off rising pipe 62 via this and flow in the corresponding coil pipe 22, and 22 effusive water liquid of the coil pipe of described processing unit 2 can be concentrated toward this cooling tank 61 via corresponding cooling water inlet pipe 64 again, and then formation circulation, in addition, this cooling tank 61 can utilize and open and close a valve 66 and the extraneous water source of control introducing, and then mediation makes, and the water liquid temp maintains design temperature (design temperature of present embodiment is 35 ℃) in this cooling tank 61.

This heat source unit 7 comprises that one is communicated with the preheated tank 41 of this preheating unit 4 and the Heat source device 71 that the water liquid in this preheated tank 41 can be heated, reach the water source unit 72 of the cooling tank 61 of this preheated tank 41 of a connection and this cooling unit 6, this water source unit 72 can carry out heat exchange with the water liquid in this preheated tank 41 and this cooling tank 61, this Heat source device 71 is city's air conditioning machinerys in the present embodiment, this Heat source device 71 utilizes the heat energy and this water source unit 72 that are produced in the cold and hot exchange process that the water liquid of this preheated tank 41 is heated to 55 ℃, and in this preferred embodiment, has only a Heat source device 71, but also a plurality of Heat source devices 71 can be set, not limited to the exposure of present embodiment according to the demand of reality.

Consult Fig. 4, this water source unit 72 has the first-class condenser 721 that is connected with cold medium, one is communicated with the expansion valve 722 of this condenser 721, one is communicated with the vaporizer 723 of this expansion valve 722, one is communicated with the compressor 724 of this condenser 721 and this vaporizer 723, one is located on this vaporizer 723 and the intensification pipeline 725 that can exchange with the cold medium heat in this vaporizer 723, reaching one is located on this condenser 721 and the cooling pipeline 726 that can exchange with the cold medium heat of this condenser 721, water liquid in this preheated tank 41 can be via this pipeline 725 that heats up, water liquid in this preheated tank 41 is heated, water liquid in this cooling tank 61 can make the water liquid cooling in this cooling tank 61 via this pipeline 726 of lowering the temperature.

In the present embodiment, the circulation of the water liquid of this multi-channel organic fertilizer treatment unit, be to utilize a plurality of pumps to carry, and control corresponding valve (figure do not show) by a plurality of temperature controlled switchs and open and close, described pump and temperature controlled switch all be not shown in graphic in, and, give unnecessary details no longer in detail at this because water route of the present utility model control is well known to those skilled in the art.

Consult Fig. 5, this multi-channel organic fertilizer treatment unit is when actual operation, water liquid in this preheated tank 41 is heated after 55 ℃ with this water source unit 72 by this Heat source device 71, these preheated tank 41 interior 55 ℃ water liquid just are delivered to the warming chamber 25 of each reactive tank 21, with the bottom of each reactive tank 21 of preheating, and season, these preheated tank 41 interior water liquid flowed in these recovery tanks 51 through this pipe connecting 52 together.

Afterwards, carry out the organic fertilizer processing operation of this reactive tank 21 of the leftmost side as shown in Figure 5, at first with the organic fertilizer charging in this reactive tank 21, its feed time is about half an hour, treat to be closed after charging finishes this reactive tank 21, make its thermal isolation, then, begin to carry out the heating steps of the organic fertilizer in this reactive tank 21, open this reactive tank 21 corresponding backwater outlet valves 54 and backwater water intaking valve 56, water liquid in this recovery tank 51 can be flowed out via corresponding backwater rising pipe 53, and through corresponding well heater 3 and being heated, water liquid after the heating flows into the coil pipe 22 of this reactive tank 21, so that behind the water liquid and the organic fertilizer heat exchange in this reactive tank 21 in this coil pipe 22, again from this coil pipe 22 via corresponding backwater water inlet pipe 55, and flow back in this recovery tank 51, so, make the water liquid after these recovery tank 51 heat exchanges, by at this recovery tank 51, backwater rising pipe 53, well heater 3, coil pipe 22, under the circulating of backwater water inlet pipe 55, the organic fertilizer in this reactive tank 21 is heated to more than 90 ℃ in about two hours.

Organic fertilizer in this reactive tank 21 is after being heated to 90 ℃, water liquid still continues to circulate in this recovery tank 51, backwater rising pipe 53, well heater 3, coil pipe 22, the backwater water inlet pipe 55, the organic fertilizer insulation that makes this reactive tank 21 is under 90 ℃ state, to react.

Consult Fig. 5, Fig. 6, organic fertilizer in this reactive tank 21 is after insulation two hours, just close the backwater outlet valve 54 and backwater water intaking valve 56 of this reactive tank 21, to stop the supply of high-temperature water liquid, and open this reactive tank 21 corresponding cooling outlet valves 63 and cooling water intaking valve 65, to carry out the cooling step of the organic fertilizer in this reactive tank 21.

Water liquid in this cooling tank 61 is after cooling off rising pipe 62 through this, and then flow into coil pipe 22 in this reactive tank 21, then, water liquid in this coil pipe 22 and the organic fertilizer in this reactive tank 21 carry out heat exchange, water liquid after the heat exchange flows out to this cooling water inlet pipe 64 from this coil pipe 22 again, and concentrate, and mix with water liquid in this cooling tank 61 toward this cooling tank 61.

Consult Fig. 4 in the lump, what deserves to be mentioned is, the water that the cooling pipeline 726 of this water source unit 72 is introduced is in the time of 35 ℃, can make the Energy Efficiency Ratio of this water source unit 72 reach the highest, and then make the water liquid that flows into this intensification pipeline 725 obtain preferable thermal efficiency, therefore, in the present embodiment, the water liquid that this cooling tank 61 is flowed in this cooling pipeline 726 via temperature control means maintains 35 ℃, and also is reduced to about 32 ℃ by these cooling pipeline 726 effusive water liquid, and then passes back in this cooling tank 61 again.

When the water liquid of this cooling tank 61 behind this cooling rising pipe 62, coil pipe 22, cooling water inlet pipe 64, by the heat that organic fertilizer absorbed in this reactive tank 21, take back in this cooling tank 61 and water liquid temp is wherein risen, at this moment, for the water liquid of regulating and control this cooling tank 61 maintains 35 ℃, understand the water liquid of opening this valve 66 and importing extraneous normal temperature, make the water liquid temp in this cooling tank 61 maintain 35 ℃ with mediation.

Water liquid in this cooling tank 61 can continue to flow in this coil pipe 22 through this cooling rising pipe 62, make the organic fertilizer heat exchange in water liquid in this coil pipe 22 and this reactive tank 21, reduce to after about 70 ℃ until the temperature of this organic fertilizer, just the organic fertilizer in this reactive tank 21 is carried out the discharging step, so just finish the slaking of these reactive tank 21 organic fertilizer.

After this reactive tank 21 (being positioned at the reactive tank 21 of left-most position as shown in Figure 5) is finished its feed step, just can carry out feed step (just being positioned at the reactive tank 21 in mid-way as shown in Figure 5) to another reactive tank 21, the charging of this reactive tank 21, heating, insulation, steps such as cooling and discharging are all identical, repeat no more in this, in like manner, the reactive tank 21 of Fig. 5 rightmost side, be after the reactive tank 21 in mid-way is finished feed step, just can carry out the processing operation of aforesaid organic fertilizer in regular turn, certainly, after each reactive tank 21 is finished its processing operation, also can repeat to implement the processing operation of identical organic fertilizer, thereby make the high-effect output that the utlity model has operation in 24 hours, really possess the high superior place of organic fertilizer treatment capacity.

By above-mentioned design, because the recovery tank 51 of this backwater unit 5 can be concentrated the water liquid by described coil pipe 22, and utilize described well heater 3 again with after the heating of water liquid, water liquid is circulated once more flow in the described coil pipe 22, thereby the heat recuperation in the water liquid is utilized again, and then can reduce the heat energy that the heating of water liquid is consumed by the round-robin means.

Moreover, the water liquid of this recovery tank 51 flows into described coil pipe 22 one by one through described well heater 3, and then in regular turn described reactive tank 21 is heated, and utilize the water liquid of this cooling tank 61 that described reactive tank 21 is lowered the temperature simultaneously, and finish the maturation operation of organic fertilizer, by the design that the utility model multi-channel organic fertilizer treatment unit is heated and lowered the temperature at multi-channel, can handle a large amount of organic fertilizer simultaneously, therefore improve the treatment capacity and the operating efficiency of organic fertilizer relatively.

And, utilize the warming chamber 25 that defines between the dividing plate 23 of each processing unit 2 and the reactive tank 21, make in this warming chamber 25 ccontaining water liquid can maintain 55 ℃ by the water liquid circulation preheating of this preheated tank 41, make these reactive tank 21 bottoms remain on 55 ℃ temperature, and avoid the dead angle that to heat.

Simultaneously, by the water liquid of this cooling tank 61 each reactive tank 21 is lowered the temperature again, not only quicken the temperature drop speed of this reactive tank 21, and also can reclaim the heat of cooling, so that this water source unit 72 can reach the running of best Energy Efficiency Ratio.

In sum, flow in the described coil pipe 22 on heating cycle ground once more by water liquid, really reach and reduce the heat energy that the heating of water liquid is consumed, and, utilize the setting of this recovery tank 51, water liquid wherein can be flowed into respectively in the corresponding coil pipe 22 via corresponding well heater 3 again, so that a plurality of reactive tanks 21 are heated, cooperate the water liquid of this cooling tank 61 in regular turn described reactive tank 21 to be lowered the temperature again, really can improve the treatment capacity and the operating efficiency of organic fertilizer, so can reach the purpose of this utility model really.

Claims (8)

1. multi-channel organic fertilizer treatment unit, it is characterized in that, this multi-channel organic fertilizer treatment unit comprises a plurality of processing units, at least one well heater that water liquid heating back is flowed into described processing unit, one is equipped with the preheating unit of water liquid, one stores the backwater unit of water liquid, one is equipped with the cooling unit of water liquid, an and heat source unit, each is handled unit pack and draws together one for the ccontaining reactive tank of organic fertilizer, reach a coil pipe that is arranged in this reactive tank, this well heater can flow into water liquid heating back in the coil pipe of described processing unit, this preheating unit comprises that one is equipped with the preheated tank of water liquid, and be placed in the coil pipe that the interior water liquid of this preheated tank can flow into described processing unit through this well heater, this backwater unit comprises that one stores the recovery tank of the effusive water liquid of coil pipe, water liquid in this recovery tank can flow into via this well heater in the coil pipe of described processing unit again and form circulation, this cooling unit comprises a ccontaining water liquid and is communicated with the cooling tank of described coil pipe, water liquid in this cooling tank can flow in the coil pipe of described processing unit, and the effusive water liquid of the coil pipe of described processing unit can be again concentrates and forms circulation toward this cooling tank, and this heat source unit is communicated with this cooling tank and this preheated tank and heats the water liquid in the preheated tank and the water liquid in the cooling tank of this cooling unit carried out heat exchange.

2. multi-channel organic fertilizer treatment unit according to claim 1, it is characterized in that, this backwater unit comprises that also one is communicated with the pipe connecting of this recovery tank and this preheated tank, the backwater rising pipe of a plurality of these recovery tanks of connection, a plurality of backwater outlet valves that are arranged on the corresponding backwater rising pipe, the backwater water inlet pipe of a plurality of these recovery tanks of connection, and a plurality of backwater water intaking valves that are arranged on the corresponding backwater water inlet pipe, each backwater rising pipe is communicated with corresponding coil pipe with each backwater water inlet pipe, and this multi-channel organic fertilizer treatment unit comprises a plurality of these well heaters that are located on the corresponding backwater rising pipe that connect.

3. multi-channel organic fertilizer treatment unit according to claim 2, it is characterized in that, each processing unit also comprises the dividing plate of the bottom of being located at this reactive tank, each handles the warming chamber that defines a ccontaining water liquid between unitary dividing plate and the reactive tank, and described warming chamber and this preheated tank are interconnected.

4. multi-channel organic fertilizer treatment unit according to claim 3, it is characterized in that, this cooling unit also comprises the cooling rising pipe of a plurality of these cooling tanks of connection, a plurality of cooling outlet valve on the corresponding cooling rising pipe, cooling water inlet pipe of a plurality of these cooling tanks of connection of being arranged on, and a plurality of cooling water intaking valves that are arranged on the corresponding cooling water inlet pipe.

5. multi-channel organic fertilizer treatment unit according to claim 4, it is characterized in that, this heat source unit comprises a Heat source device that is communicated with this preheated tank and the water liquid in this preheated tank can be heated, reach one and be communicated with this preheated tank and this cooling tank, the water source unit that carries out heat exchange with water liquid the water liquid in the cooling tank and this preheated tank.

6. multi-channel organic fertilizer treatment unit according to claim 5, it is characterized in that, this water source unit have that vaporizer, that expansion valve, that the first-class condenser that is connected with cold medium, is communicated with this condenser is communicated with this expansion valve is communicated with that this condenser and the compressor, of this vaporizer are located on this vaporizer and can with the intensification pipeline of cold medium heat exchange in this vaporizer, reach one be located on this condenser and can with the cooling pipeline of the cold coal heat exchange of this condenser.

7. multi-channel organic fertilizer treatment unit according to claim 6, it is characterized in that, each well heater has a tubular body, and is arranged at the inner ring surface of this tubular body and is arranged at the inner ring surface of this tubular body and second electric-conductor that is connected with the negative electricity of this power supply with first electric-conductor, that the positive pole of a power supply is electrically connected at intervals with this first electric-conductor, reaches two earthings that link to each other with this tubular body respectively and is arranged at the separator of two end opposite of this tubular body.

8. multi-channel organic fertilizer treatment unit according to claim 7 is characterized in that, each processing unit comprises that also one is arranged in this reactive tank in order to stir the agitator of organic fertilizer.

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