CN1705625A

CN1705625A - Compost, and method and apparatus for producing the same

Info

Publication number: CN1705625A
Application number: CNA200480001310XA
Authority: CN
Inventors: 野口和利
Original assignee: Individual
Current assignee: Individual
Priority date: 2004-02-23
Filing date: 2004-02-23
Publication date: 2005-12-07
Also published as: WO2005080296A1

Abstract

An apparatus (A) for producing a compost which comprises a feces and urine supplying device (6), a wallastonite supplying device (7), a conc. sulfuric acid supplying device (8), a feces and urine agitating device (1, 1a), a feces and urine reactor (2) for mixing a mixture from the feces and urine agitating device (1, 1a) with sulfuric acid supplied from a tank, a fowl droppings reactor (3) for mixing and agitating fowl droppings and a wallastonite supplied from a tank and further mixing and agitating the resultant mixture with sulfuric acid, to react them, and a fermentation device for adding an effective microbe to respective mixtures formed by the mixing and agitation in the feces and urine reactor (2) and the fowl droppings reactor (3). The apparatus can be used for reacting feces and urine of a pig or a human being or the like with wallastonite and conc. sulfuric acid, to convert them to a solid or a particulate material and reduce a bad odor, and further for achieving with sure their fermentation by a microbe, i.e. their conversion to a compost also in a practical and large scale case.

Description

Compost and manufacture method thereof and manufacturing installation

Technical field

The present invention relates to compost and manufacture method thereof and manufacturing installation.In more detail, related is is using pig manure urine or human excrement and is mixing with siliceous wollastonite and when making compost, can make the fermentation based on effective microbe is that composting goes on conscientiously.

Technical background

As everyone knows, silicon (Si) is collected in the cell walls of most plants, is one of important element to plant.

The Okinawa Prefecture that the inventor lived, the harvest yield of sugarcane reduces year by year.It is generally acknowledged that its reason is: soil is subjected to polluting certainly needless to say because of chemical fertilizer and weedicide etc., a large amount of silicon and other trace element run off from soil together or take out of by crop, cause silicone content in the soil not enough and make that soil fertility is whole to descend.

In fact, the dregs that sugarcane has been pressed adhere to white silicic acid in a large number as the facilities such as boiler of fuel in roasting kiln, reached the degree that must remove operation.Also infer easily thus: can not ignore the amount that the silicon in the soil is taken out of because of crop.Even the soil cultivated plant that this soil fertility is low can not gathered in the crops fully because stem is thick, leaf is not wealthy yet.

But though there is the deficiency of silicon in the soil, if for example diatomite merely being sneaked under becoming the state of powder in the soil as the silicon of inorganics, then crop can not absorb fully.For silicon is absorbed by crop, must make to have Ionized silicon in the soil.

The inventor is in order to realize the ionization of silicon, carried out all the year round research repeatedly.And in experiment, learn: silicon is mixed with organism, and then and strong sulfuric acid response, can promote the ionization of element silicon thus, if apply fertilizer after making its composting, then have the effect of recovering soil fertility.

But, swine rearing number in Okinawa is many, and handling pig manure urine is a big problem.Pig manure urine is organism, and the inventor just is conceived to handle this pig manure urine.

In addition, handle, proposed various methods so far really and implement, disclose the method (opening flat 10-152385 communique) of using siliceous wollastonite acquisition organic fertilizer with reference to the spy for carrying out fecaluria.

Open the manufacture method of the organic fertilizer of flat 10-152385 communique record according to the spy, can be reflected at that (or moment) makes the high waste liquids such as domestic animals manure of water ratio realize solid shapeization or spheroidizing in the extremely short time by natural wollastonite and vitriolic, thereby stink is improved, and then utilize reaction heat that nearly all assorted bacterium is killed, thereby the also easy thereafter fertilizerization (composting) that realizes adding effective microbe and carry out.

Whether the manufacture method that the inventor adopts above-mentioned spy to open the organic fertilizer of flat 10-152385 communique record is confirmed using pig manure urine or human excrement to form compost, the result has obtained following opinion: at least aspect the real standard of a large amount of processing fecalurias, even add effective microbe through also not fermentation in four months, thereby can not make compost.

So the inventor is that purpose has been carried out all tests with the fermentation, the result has obtained following opinion: if add chicken manure, even adopt aforesaid method also can ferment.Though its reason is also unclear, it is generally acknowledged that the composition of chicken manure is relevant with the effective microbe fermentation activity.

The present invention is based on such opinion and finishes.

Summary of the invention

The object of the present invention is to provide a kind of compost, this compost can be cultivated good crop by improving the fertility of soil, can also increase output.

Another object of the present invention is to provide a kind of manufacture method of compost, when making compost, can be reflected at by wollastonite and vitriolic makes the high fecaluria of water ratio realize solid shapeization or spheroidizing in the extremely short time, thereby stink is improved, even simultaneously aspect the big real standard of treatment capacity, also the fermentation that can carry out conscientiously based on effective microbe is a composting.

A further object of the present invention is to provide a kind of manufacturing installation of compost, when producing compost, can be reflected at by wollastonite and vitriolic makes the high fecaluria of water ratio realize solid shapeization or spheroidizing in the extremely short time, thereby stink is improved, even simultaneously aspect the big real standard of treatment capacity, also the fermentation that can carry out conscientiously based on effective microbe is a composting.

In order to achieve the above object, the technical scheme of being narrated of the present invention is as follows.

The 1st invention is:

A kind of compost, it is characterized in that: described compost obtains by following method: mix wollastonite in pig manure urine or human excrement, then mixes and react and make it curing or spheroidizing with the vitriol oil, in the material that obtains like this, be blended in and mix wollastonite in the chicken manure, then mix and make it to react and solidify or the material of spheroidizing with the vitriol oil, with this mixture is substratum, adds effective microbe and makes it fermentation.

The 2nd invention is:

A kind of compost manufacture method, it is characterized in that: in pig manure urine or human excrement, mix wollastonite, then mixes and react and make it curing or spheroidizing with the vitriol oil, in the material that obtains like this, be blended in and mix wollastonite in the chicken manure, then mix and make it to react and solidify or the material of spheroidizing with the vitriol oil, with this mixture is substratum, adds effective microbe and makes it fermentation.

The 3rd invention is:

Manufacture method according to the 2nd compost of inventing, it is characterized in that: the wollastonite that in the pig manure of 100 weight parts urine or human excrement, mixes 10～25 weight parts, then mixes and react and make it curing or spheroidizing with the vitriol oil of 5～15 weight parts, in the material of 100 weight parts that obtain like this, be blended in mix in the chicken manure wollastonite, then mix with the vitriol oil and make it to react and solidify material 15 weight parts of spheroidizing or more than, with this mixture is substratum, adds effective microbe and makes it fermentation.

The 4th invention is:

Compost manufacture method according to the 2nd or the 3rd invention is characterized in that: add a kind of selecting among zinc (Zn), manganese (Mn), molybdenum (Mo), magnesium (Mg), copper (Cu), the iron (Fe), two or more.

The 5th invention is:

A kind of compost manufacturing installation is characterized in that it has: the fecaluria feedway of supplying with pig manure urine or human excrement; Supply with the wollastonite feedway of wollastonite; Supply with the vitriol oil feedway of the vitriol oil; The pig manure urine supplied with or human excrement and wollastonite are mixed the fecaluria whipping appts that stirs; To mix the mixture that stirred by the fecaluria whipping appts and be mixed the fecaluria reaction machine that stirs and make it to react with the vitriol oil of being supplied with; Mix and stir chicken manure and wollastonite, and then in its mixture, mix the chicken manure reaction machine that stirs the vitriol oil and make it to react; The fermentation unit that in the mixture of the material that gets by fecaluria reaction machine and chicken manure reaction mechanism, adds effective microbe and make it to ferment.

The 6th invention is:

Compost manufacturing installation according to the 5th invention is characterized in that: fecaluria reaction facility have worm conveyor, are used for carrying while stirring the mixture that is mixed with mixed stirring and the material of the vitriol oil; And the part of mixing the vitriol oil is arranged on the transfer base side of worm conveyor or leads to the giving in the passage of mixture of transfer base side.

The 7th invention is:

Manufacturing installation according to the 5th or the 6th compost of inventing, it is characterized in that: the wollastonite feedway has the device of giving, describedly give device and be provided with a plurality of fecaluria whipping apptss at least and be connected, and supply with wollastonite selectively to each fecaluria whipping appts, the stink in the fecaluria whipping appts can outwards not leaked from supplying with part.

Wollastonite (Wallastonite, Calucium Silicate powder, CaSiO ₃) can be natural also can be synthetic.

With respect to the pig manure urine or the human excrement of 100 weight parts, the blending ratio of wollastonite is 10～25 weight parts, is preferably 15～18 weight parts.Equally, the blending ratio of the vitriol oil is 5～15 weight parts, is preferably 8～10 weight parts.

When wollastonite less than 10 weight parts or vitriol oil less than 5 weight parts, curing or spheroidizing can not be carried out fully, and temperature of reaction is also low, and assorted bacterium can residually be arranged.

In addition, even when wollastonite surpasses 25 weight parts or the vitriol oil and surpasses 15 weight parts, solidify or the degree of spheroidizing and temperature of reaction aspect almost do not change yet, so the wollastonite and the vitriol oil only are surplus is arranged and to cause waste.In addition, when wollastonite surpasses 25 weight parts, then too hard and make and handle the difficulty that becomes.

Moreover, in chicken manure, mix the wollastonite and the vitriol oil and make it to react and solidify or the blending ratio of the material of spheroidizing be 15 weight parts or more than, if less than 15 weight parts, even add effective microbe, fermentation can not be carried out fully.

With respect to the chicken manure of 100 weight parts, the blending ratio of wollastonite is 5～12 weight parts, is preferably 7～10 weight parts.Equally, the blending ratio of the vitriol oil is 3～8 weight parts, is preferably 5～6 weight parts.

When wollastonite less than 5 weight parts or vitriol oil less than 3 weight parts, curing or spheroidizing can not be carried out fully, and temperature of reaction is also low, and assorted bacterium can residually be arranged.

In addition, even when wollastonite surpasses 12 weight parts or the vitriol oil and surpasses 8 weight parts, solidify or the degree of spheroidizing and temperature of reaction aspect almost do not change yet, so the wollastonite and the vitriol oil only are surplus is arranged and to cause waste.In addition, when wollastonite surpasses 12 weight parts, then too hard and make and handle the difficulty that becomes.

Can list aerobic and anaerobic microorganism as the effective microbe that makes fermented mixture (zymophyte), for example lactobacillus (bacillus bifidus etc.), yeast flora (aspergillus tubigensis etc.), photosynthetic bacterium group (bead phycomycete etc.), the thread flora of fermentation class, Gram positive actinomycetes group etc., but be not limited to these microorganisms.

The present invention brings into play following effect.

Pig manure urine or human excrement and chicken manure are stored in the reservoir such as jar in right amount.In addition, the wollastonite and the vitriol oil also are stored in the reservoir such as jar in right amount.Then, for example in wollastonite, add an amount of be selected among zinc (Zn), manganese (Mn), molybdenum (Mo), magnesium (Mg), copper (Cu), the iron (Fe) a kind, two or more.

Pig manure urine or human excrement input or give in the fecaluria whipping appts.When an amount of storage has fecaluria in the fecaluria whipping appts, cooperate wollastonite and mix stirring by predetermined proportion.

In the mixture that adopts the mixing of fecaluria whipping appts to stir, mix the vitriol oil, in fecaluria reaction machine, stir and make it reaction.

By this reaction (wollastonite and strong sulfuric acid response), mixture solidifies or spheroidizing in the short period of time at the utmost point, and the distinctive stink of fecaluria is improved.In addition, produce reaction heat, mixture temperature reaches 75～85 ℃, almost kills the assorted bacterium that contains harmful bacterium such as pathogenic bacteria that exists in the mixture.

On the other hand, the chicken manure input or give chicken manure reaction machine.When an amount of storage has chicken manure in the chicken manure reaction machine, cooperate wollastonite and mix stirring by predetermined proportion.

Moreover, in this mixture, mix the vitriol oil, in chicken manure reaction machine, stir and make it reaction.By this reaction, mixture similarly solidifies or spheroidizing with the situation of handling pig manure and human excrement, and stink also is improved, and can kill assorted bacterium by reaction heat.

When being cooled to proper temperature (the propagable temperature of effective microbe) when the mixture that makes by pig manure urine or human excrement with by the mixture that chicken manure makes, they are mixed, add effective microbe, utilize the ferment tank preset time and make it composting.In addition, also can after mixing, cool off.

Because several flat assorted bacterium that contain harmful bacterium such as pathogenic bacteria that do not exist so the effective microbe that adds can fully activate, can be made the fine compost efficiently in each mixture.

In addition, the blended material for example can use various transfer rollers such as worm conveyor and endless belt conveyor to carry out to the conveying of fermentor tank, perhaps uses overhead driving that containers such as transport box mode such as carry is carried out.

Fecaluria of the present invention reaction facility have worm conveyor, are used for carrying while stirring being mixed with the mixture that was stirred and the material of the vitriol oil; And the part of mixing the vitriol oil is arranged on the transfer base side of worm conveyor or leads to the giving in the passage of mixture of transfer base side.According to fecaluria reaction machine of the present invention, for mixing the vitriol oil, press equipressure, so device can be simplified because need hardly to inject.

That is to say that it is by utilizing the screw rod rotation to make mixture continuously to carrying rear portion side (discharge side) to move the part that produces negative pressure that the transfer base side of worm conveyor or the mixture that leads to the transfer base side are given passage.Therefore, the vitriol oil can effectively mix in the mode that sucks.

Moreover, because the vitriol oil mixes in the transfer base (carrying anterior) of worm conveyor, thereby mixture carries rear portion (outlet side) just can stir fully before being sent to, the wollastonite and the vitriol oil react earlier, say on the whole roughly to be cured equably and spheroidizing.Thus, can carry out the manufacturing of compost effectively.

The device of giving of the present invention is provided with a plurality of fecaluria whipping apptss at least, and supplies with wollastonite selectively to each fecaluria whipping appts, and the stink in the fecaluria whipping appts can outwards not leaked from supplying with part.According to the device of giving of the present invention, for example when a side fecaluria whipping appts carries out stir process etc., can be transported to the opposing party's fecaluria whipping appts to fecaluria and wollastonite to descend the preparation of subjob.Thus, the manufacturing of compost can be carried out effectively, and pig manure urine or human excrement can be handled effectively.

In addition, because the stink of the pig manure of giving birth to urine or human excrement in fact can be to external leaks, thereby also can prevent the deterioration of the operating environment that causes because of stench and the trouble of bringing to the surrounding area.

Description of drawings

Fig. 1 is the schematic plan view of an embodiment of expression compost manufacturing installation of the present invention.

Fig. 2 is the diagrammatic side view of an embodiment of expression compost manufacturing installation.

Fig. 3 is that the master of expression fecaluria whipping appts structure looks cross sectional illustration figure.

Fig. 4 is the explanatory view of overlooking of expression fecaluria whipping appts structure.

Fig. 5 is the side-looking explanatory view of expression fecaluria whipping appts structure.

Fig. 6 is that the A-A of Fig. 3 is to part sectioned view.

Fig. 7 is the cross sectional illustration figure of a part that drops into the rotary valve arrangements of wollastonite to two fecaluria whipping apptss selectively.

Fig. 8 is the cross sectional illustration figure of expression fecaluria reaction machine structure.

Fig. 9 is that the master of expression chicken manure reaction machine structure looks cross sectional illustration figure.

Figure 10 be expression chicken manure reaction machine structure overlook cross sectional illustration figure.

Figure 11 is the side-looking cross sectional illustration figure of expression chicken manure reaction machine structure.

Figure 12 is the explanatory view of the opening and closing structure of expression chicken manure reaction machine discharging lid.

Figure 13 is the orthographic plan of expression compost of the present invention manufacturing works outline.

Embodiment

With illustrated embodiment serves as that the basis is described in detail with regard to the present invention.

Fig. 1 is the schematic plan view of an embodiment of expression compost manufacturing installation of the present invention;

The fermentation unit 4 that constitutes the compost manufacturing installation is illustrated among Figure 13 for simplicity.

In Fig. 1, Fig. 2, fecaluria reaction machine 2 is illustrated in the outside of frame 9 for simplicity.The part of wollastonite feedway 7 and the diagram of vitriol oil feedway 8 have been omitted among Fig. 2.

Fig. 3 is that the master of expression fecaluria whipping appts structure looks cross sectional illustration figure;

Fig. 4 is the explanatory view of overlooking of expression fecaluria whipping appts structure;

Fig. 5 is the side-looking explanatory view of expression fecaluria whipping appts structure;

Fig. 6 is that the A-A of Fig. 3 is to part sectioned view;

Fig. 7 is the cross sectional illustration figure of a part that drops into the rotary valve arrangements of wollastonite to two fecaluria whipping apptss selectively;

Fig. 8 is the cross sectional illustration figure of expression fecaluria reaction machine structure;

Fig. 9 is that the master of expression chicken manure reaction machine structure looks cross sectional illustration figure;

Figure 10 be expression chicken manure reaction machine structure overlook cross sectional illustration figure;

Figure 11 is the side-looking cross sectional illustration figure of expression chicken manure reaction machine structure;

In addition, Figure 13 is the orthographic plan of outline of the compost manufacturing works of the expression compost manufacturing installation that comprises the present embodiment.

As Fig. 1, shown in Figure 3, the compost manufacturing installation A of the present embodiment has: fecaluria feedway 6; Wollastonite feedway 7; Vitriol oil feedway 8; Mix the fecaluria whipping appts 1, the 1a that stir fecaluria (pig manure urine or human excrement) and wollastonite; Mix to stir by

fecaluria whipping appts

1,1a and mix the mixture that stirred and react machine 2 by the vitriol oil of jar supply and the fecaluria that makes it to react; Mix the wollastonite that stirs chicken manure and supply with, and then in its mixture, mix the chicken manure reaction machine 3 that stirs the vitriol oil and make it to react by jar; Adopting fecaluria reaction machine 2 and chicken manure reaction machine 3 to mix the fermentation unit 4 (referring to Figure 13) that adds effective microbe in the stirred mixture and make it to ferment respectively.

In addition, above-mentioned each one of compost manufacturing installation A is for preventing corrosion, and the metal of mainly adopt stainless steel or other uncorruptible metal, having implemented antirust processing waits to be made, also can compound use synthetic resins etc. other starting material.

(

fecaluria whipping appts

1,1a)

Mainly with reference to Fig. 3 to Fig. 7.

Fecaluria whipping appts

1,1a are arranged on the top of the private side of frame 9.

Fecaluria whipping appts

1,1a supply with fecaluria by fecaluria feedway 6, supply with wollastonite by wollastonite feedway 7.Fecaluria feedway 6 and wollastonite feedway 7 (all being illustrated among Fig. 1) describe in the back.

The structure of frame 9 is: four jiaos have pillar 90, connect these pillars 90 in length and breadth by transom 91, and the bottom are provided with base plate 94.In the upper end of each pillar 90, be provided with operation scaffolding 92 in the mode of surrounding each pillar 90.Around operation scaffolding 92, be provided with handrail 93.

Fecaluria whipping appts

1,1a have stirred pot 10 respectively and are located at stirrer 12 on the stirred pot 10.

Each stirred pot 10 is fixed on the transom 91 of upper side, and is set up in parallel with same height.In addition,

fecaluria whipping appts

1,1a have roughly same structure, so for detailed structure, will describe with the fecaluria whipping appts 1 that is shown in Fig. 3 right side and expresses internal structure.In addition, the symbol identical with each one of fecaluria whipping appts 1 represented on each standard laid down by the ministries or commissions of the Central Government of fecaluria whipping appts 1a.

Stirred pot 10 be cylindric, the upper and lower is sealed in fact (except each introducing port, the relief outlet) jar.

Inboard (side of the opposing party's stirred pot 10) at the top panel 101 of stirred pot 10 is provided with the ingress pipe 102 that is connecting pipe connecting 112 described later, is used for the inside that wollastonite is fed to jar.In addition, the opposition side in the inboard is provided with window 103 to be opened/closed, situation or keep in repair in being used for observing jar.

In addition, the central part of plate 101 is provided with assembling pipe 104 in the above, is used to be provided with stirrer 12 described later.

The central part of the bottom panel 105 of stirred pot 10 is provided with vent pipe 106, is connected on the vent pipe 106 giving pipe 108 by valve 107.

Give pipe 108 and be connected the interflow, be connected on the fecaluria reaction machine 2 described later by supply-pipe 109 with the pipe 108 of giving of the opposing party's fecaluria whipping appts 1a.

Stirrer 12 has motor 120.Motor 120 is fixed on the assembling pipe 104, and the turning axle 121 of stirrer vertical direction downwards extends.Turning axle 121 lower end are on than the position of bottom panel 105 above slightly.The bottom of turning axle 121 is provided with the agitating screw 122 of four blades.

In addition, in the outside of agitating screw 122, cylindric stirring control volume 123 is being set in the mode of surrounding agitating screw 122.Agitating screw 122 is positioned at the lower side that stirs control volume 123, and its top ends is provided with at interval so that make it and does not contact with stirring control volume 123.Stirring control volume 123 is fixed on the side panel 110 of above-mentioned stirred pot 10 by stay 111.

In addition, because make agitating screw 122 to rotate to the mode of carrying fecaluria upward, institute thinks the raising stirring efficiency, preferably makes the height of agitating screw 122 be positioned at downside, but does not limit its height.

According to above-mentioned stirring control volume 123, be the boundary with the sidewall that stirs control volume 123, the inboard and outside is when stirring, and fecaluria mobile is difficult to cause the phase mutual interference, and flow upward in the inboard, and the outside is then mobile downwards.That is to say, can be as not establishing the situation that stirs control volume 123, drive the rotation of fecaluria integral body by the rotation of agitating screw 122, its advantage is to make to stir is carried out conscientiously.

With reference to Fig. 1.

Fecaluria feedway 6 has closed fecaluria jar 60.Between fecaluria jar 60 and above-mentioned each stirred pot 10, be provided with and give pipe 61, be used for the fecaluria of fecaluria jar 60 inside is flowed to each stirred pot 10.In the path of giving pipe 61, be provided with pump (omitting among the figure).In addition, the stink of fecaluria jar 60 inside manages 65 by having giving of topping-up pump 650, just is fed to the bottom of the fermentor tank 40 of aftermentioned fermentation unit 4.

In addition, give pipe each stirred pot 10 side of 61 along separate routes by switching valve 62, along separate routes give the top that

pipe

63,64 imports to each stirred pot 10 separately.

What wollastonite feedway 7 had sealed wollastonite jar 70 and was located at stirred pot 10 tops gives device 72.

The lower side of wollastonite jar 70 forms funnel-form, makes the discharge of wollastonite become easy.On the discharge portion of being located at wollastonite jar 70 bottoms, connecting be used for conveying powdered wollastonite give transfer roller 71, the end of giving transfer roller 71 imports to the above-mentioned device 72 of giving.

In addition, with respect to employed fecaluria amount (hold-up in the stirred pot 10), the wollastonite of necessary mix predetermined quantities.Therefore, wollastonite feedway 7 has the measurement means that the wollastonite of carrying is measured.

As this measurement means, for example can adopt following mode to wait carries out: be provided with weight sensor on the part that supports wollastonite jar 70 (as the leg frame etc.), the weight that contains the whole wollastonite jar 70 of wollastonite by metering, obtain the wollastonite amount of giving, the control device that is reflected to operational throughput is then controlled, but the present invention is not limited thereto.

In addition, on wollastonite jar 70, be provided with and preventing the build bridge means of (hopper bridge: form blank part near the stock relief outlet and cause discharging difficult phenomenon) of so-called hopper.There is no particular limitation to these means, for example can adopt following various known means: 1. dispose vibrator, utilize vibration to make stock defeated and dispersed; 2. give inner spray air, utilize blast to make stock defeated and dispersed; 3. in inner face side plate body is set, this plate body cover air ejiction opening and make it to have connect from may (can swing).

Mainly with reference to Fig. 7 and Fig. 3.

Giving device 72 is arranged on the vent pipe 730 that makes whirlwind aggregate tube 73 bottoms that wollastonite falls downwards.On the top of whirlwind aggregate tube 73, be provided with and make the wollastonite that is imported at inner dispersive gas blower 731.

Give device 72 when wollastonite being supplied to each

fecaluria whipping appts

1,1a selectively, can not make the stink in fecaluria whipping appts 1, the 1a leak into the outside from supplying with part.

Give device 72 and have shell 720, shell 720 has and is circular-arc perisporium 721,722 on front view top ground, and face side and rear side are actually sealing.Part beyond the perisporium 721,722 constitutes the introducing port 723 of upper side and the relief outlet 724,725 of both sides, bottom.

Introducing port 723 is provided with the narrow slightly ingress pipe 723a of lower side, and the top of ingress pipe 723a is connected on the vent pipe 730 of whirlwind aggregate tube 73.

In addition, in the relief outlet 724,725

vent pipe

724a, 725a are being set,

vent pipe

724a, 725a are connecting the pipe connecting 112 that the lower side bending is " く " sigmoid respectively.The bottom of pipe connecting 112 is connected on the ingress pipe 102 of above-mentioned each stirred pot 10.

The inner face that the inboard of above-mentioned shell 720 is close to shell 720 is being provided with the slidably switching valve 726 of rotation.Switching valve 726 has short valve 726a of portion and the long valve 726b of portion, the girth of its short-and-medium valve 726a of portion is identical with perisporium 721 (or perisporium 722), and the girth of the long valve 726b of portion is longer than the girth that perisporium 721 (or perisporium 722) and relief outlet 724 (or relief outlet 725) are lumped together slightly.

Switching valve 726 as shown in Figure 7, half is close to perisporium 722, bottom half stops up state that relief outlet 725 and the short valve 726a of portion be close to perisporium 721 half is close to perisporium 721, bottom half stops up the state that relief outlet 724 and the weak point valve 726a of portion are close to perisporium 722 approximately approximately to long valve portion 726b top approximately approximately from the top of the long valve 726b of portion, switching valve can rotate in a circumferential direction (revolution).

Utilize the rotation (revolution) of this switching valve 726, can between relief outlet 724 that becomes the importing side or relief outlet 725, switch.

The inboard of switching valve 726 is provided with rotary valve 727.Rotary valve 727 has rotation central siphon 727a, and its peripheral part circumferentially equally spaced is provided with the five valve plate 727b of place.Valve plate 727b is arranged at radially, so that make each top ends can be close to the long valve 726b of portion of switching valve 726 and the inner face of the short valve 726a of portion slides.

Utilize this structure, can be with at the stirred pot 10 of the wollastonite that falls between the valve plate 727b of top below the relief outlet 724 opened or relief outlet 725 guiding.In addition, the inner face of the top ends of each valve plate 727b and the long valve 726b of portion and the short valve 726a of portion roughly is close to, during rotary valve 727 rotations, where no matter valve plate 727b be in, and always has a certain valve plate 727b can block the ventilation of 10 of each stirred pots of whirlwind aggregate tube 73 and

fecaluria whipping appts

1,1a.

Therefore, in fact the pig manure urine of giving birth to or the stink of human excrement can not leak into the outside of each stirred pot 10, thereby also can prevent the deterioration of the operating environment that causes because of stench and the trouble of bringing to the surrounding area.

In addition, the rotation of the revolution of switching valve 726 and rotary valve 727 is controlled by not shown control device.

(fecaluria reaction machine 2)

Mainly with reference to Fig. 8, figure (a) is overall description figure, and Fig. 8 (b) is the cross sectional illustration figure of expression take-off pipe connection section structure.

Fecaluria reaction machine 2 is arranged on the below of fecaluria whipping appts 1,1a.Fecaluria reaction machine 2 has horizontally disposed worm conveyor 20, and worm conveyor 20 has pipe 201 and screw rod 202, and screw rod 202 drives rotation by motor 21.Top ends at pipe 201 is being provided with pipe connecting 26.In addition, pipe 201 is fixed on the base plate 94 by permanent joint 25.

The top of the base portion side of pipe 201 is provided with ingress pipe 22.It is sulfuric acid ingress pipe 23 that the top of ingress pipe 22 is connecting the part that is used to import the vitriol oil.Sulfuric acid ingress pipe 23 is connected with spherical joint 24 by the supply-pipe 109 that is arranged on above-mentioned

fecaluria whipping appts

1,1a discharge side.

Supply with the vitriol oil from vitriol oil feedway 8 (being illustrated in Fig. 1) to fecaluria reaction machine 2.Vitriol oil feedway 8 has vitriol oil jar 80, is being provided with between the sulfuric acid ingress pipe 23 of vitriol oil jar 80 and fecaluria reaction machine 2 and is giving pipe 81.In the path of giving pipe 81, be provided with pump 82.

The tip side of giving pipe 81 is connected on two side's ramose injection tubes 83.Two take-off pipes 830 of injection tube 83 connect and import in two place's sidewalls 230 that sulfuric acid pipe 23 footpaths make progress.And fixedly installing traverse baffle 231 in the inner face side of sidewall 230, this traverse baffle leaves top end opening portion that distance a bit covers take-off pipe 830 slightly from the top, and at lower side (giving the direction side) opening (with reference to Fig. 8 (b)).

According to this structure, because the pressure of the mixture of carrying by sulfuric acid ingress pipe 23, discharge from arbitrary stirred pot 10 of

fecaluria whipping appts

1,1a is difficult to act on take-off pipe 830 top end opening portions, so, even without applying king-sized pressure, also can successfully carry out the injection of the vitriol oil.In addition, do not need the pneumatic plant of exerting pressure etc. thus to the injection of the vitriol oil, thus can simplification device, and manufacturing cost also can be suppressed on the cheap level.

The pipe connecting 26 of fecaluria reaction machine 2 top ends is connected the base portion side of worm conveyor 27.The tip side of worm conveyor 27 is extended obliquely upward, can be from top fecaluria cast and be housed in be disposed at

fecaluria whipping appts

1,1a rear conveying with in the container 5 (being illustrated in Fig. 1, Fig. 2).

In addition, carry bottom to have cast mouthful (omitting diagram and symbol) to be opened/closed with container 5.If be detained the mixture that predetermined amount is arranged, then mixture connects container and is transported to fermentor tank 40 together, drops into from the input port.In addition, mixture also can be in the maintenance of carrying with process certain hour in the container 5 before dropping into fermentor tank 40.

(chicken manure reaction machine 3)

Mainly with reference to Fig. 9 to Figure 12.Chicken manure reaction machine 3 is configured in the rear (among Fig. 1 at upside) of

fecaluria whipping appts

1,1a.

Chicken manure reaction machine 3 has stirrer 30 and wollastonite feedway 31 and vitriol oil feedway 32.

Stirrer 30 has stirred pot 33, the sealing of this stirred pot upper opening and both ends, and section roughly is U word shape, and has desired length.Stirred pot 33 is by bracing member 34 horizontal supports that all around are provided with everywhere.The edge portion of stirred pot 33 tops one side's length direction is installed with lid 35, and this lid can open and close peristome and can rotate.

In addition, symbol 350 expression gas block panels, this gas block panel hinders the on-off action of lid 35 to prevent rapid activity.

The bottom of the length direction central part of stirred pot 33 is provided with tetragonal conveying end 330.The exterior side of stirred pot 33 is being provided with by sliding can open and close the lid 331 of conveying end 330.The design that lid 331 adopts along conveying end 330 bent around shape bendings.The design that lid 331 is adopted is can move on the direction in week and can slide about shown in Figure 11,12 along the guide rail 332 that is arranged at conveying end 330 both sides.

Lid 331 opens and closes (also can adopt cylinder) by hydro-cylinder 333.The piston masthead of hydro-cylinder 333 (rod head) is supported on the lid 331 with mode axle free to rotate.In addition, cylinder portion also is supported on the installation accessory 334 that is fixed on the stirred pot 33 with mode axle free to rotate.According to this structure, utilize the piston rod flexible (advance and retreat) of hydro-cylinder 333, lid 331 is is successfully opened and closed move.

The inner bottom part of stirred pot 33 is being provided with screw mixer 36.Screw mixer 36 has screw rod 361, and screw rod is supported on the length direction of stirred pot 33 with mode axle free to rotate by bearing 360.Screw rod 361 has peripheral part diameter difference and the also different two kinds of blades (having omitted symbol separately) of the hand of spiral.In addition, the big directly blade construction of side is that peripheral part rotates in the mode that almost contacts stirred pot 33 inner bottom surfaces.

According to this structure, in one direction rotation simultaneously the left and right directions in Fig. 9,10 to stir mobile handled thing and carry out that continuous round-robin stirs be possible, and stir and can be carried out effectively.

After step-down gear 363 and sprocket wheel deceleration, the motivating force of motor 362 is passed to screw rod 361, wherein motor 362 is assemblied on the stand member 335 of being located at stirred pot 33 1 distolateral places.

Above-mentioned wollastonite feedway 31 has wollastonite jar 310, and a distolateral bottom that is connected wollastonite jar 310 of worm conveyor 311 is so that can fetch in wollastonite.The distolateral peristome edge portion that is arranged on stirred pot 33 along its length of another of worm conveyor 311.In addition, body (symbol omission) lower side corresponding to the part of peristome is provided with a plurality of input ports (symbol omission).

The other end of worm conveyor 311 is positioned at the end of stirred pot 33, and inner spiral (diagram is omitted) drives rotation by motor 312.In addition, the axle of screw rod and blade are to have flexible flexure member, and body bend office also can rotate.

The stink that reactant gases etc. is contained in stirred pot 33 inside is given pipe 37 by what have a gas blower 370, can be transported to the bottom of the fermentor tank 40 of aftermentioned fermentation unit 4.

Above-mentioned vitriol oil feedway 32 has near the vitriol oil jar of being located at the wollastonite jar 310 320.Between one distolateral (right side among Fig. 9, Figure 10) of vitriol oil jar 320 and above-mentioned stirred pot 33, be provided with and give pipe 321.In the path of giving pipe 321, be provided with the pump 322 that to carry the vitriol oil, can quantitatively flow to stirred pot 33 to the vitriol oil by pump 322.

(fermentation unit 4)

With reference to Figure 13.

As shown in the figure, fermentation unit 4 is located at and fecaluria whipping appts 1, the isolating place of 1a.Fermentation unit 4 has fermentor tank 40 and mobile whipping appts 41, and wherein mobile whipping appts 41 moves back and forth and stir inner mixture along the sidewall of fermentor tank 40, and to discharging the side conveying.In fermentor tank 40, handled thing not only, and also carry out fermentative processing together from the stink that fecaluria jar 60 and chicken manure reaction machine 3 are sent.

In addition, the fermentation unit 4 with fermentor tank 40 and mobile whipping appts 41 is because of being known extremely general structure, thereby omits its detailed description.

(effect)

With reference to Fig. 1～Figure 13, the effect of compost manufacturing installation and compost manufacturing works is described.

Pig manure urine or human excrement are stored in the fecaluria jar 60 in right amount, also chicken manure are stored in right amount as required in the storage portion such as jar.

In addition, an amount of storage wollastonite also stores the vitriol oil in right amount in vitriol oil jar 80 in wollastonite jar 70.An amount of in wollastonite (being generally trace) add a kind of being selected among zinc (Zn), manganese (Mn), molybdenum (Mo), magnesium (Mg), copper (Cu), the iron (Fe), two or more.This is in order to replenish enough mineral substance in compost.Usually preferably add above-mentioned all categories, but also can add the kind of suitably selecting, and its proportioning also can suitably be adjusted not special restriction in conjunction with the soil regime of fertilising etc.

Pig manure urine or human excrement are transported in each stirred pot 10 of

fecaluria whipping appts

1,1a selectively.When in each stirred pot 10 an amount of storage being arranged, give a side stirred pot 10 or the opposing party's stirred pot 10 supply wollastonites by the device 72 of giving of wollastonite feedway 7.Wollastonite is allocated in the ratio of 15 weight parts with respect to the fecaluria of 100 weight parts, mixes stirring by stirrer 12.

Open valve 107, carry to fecaluria reaction machine 2 mix the mixture that stirred with

fecaluria whipping appts

1 or 1a.

Inject the sulfuric acid ingress pipe 23 of fecaluria reaction machine 2 from two sides in opposite directions by injection tube 83 by the vitriol oil of vitriol oil feedway 8 supplies.The vitriol oil is allocated in the ratio of 8 weight parts with respect to the fecaluria of 100 weight parts.

Mixed the mixture of the vitriol oil and then flowed to worm conveyor 20, be transported to the discharge side while in pipe 201, mix stirring by screw rod 202.

Stir the mixture and the vitriol oil by mixing, chemical reaction just takes place in the wollastonite and the vitriol oil of sneaking in the mixture.

Utilize this reaction, mixture solidified or spheroidizing in the utmost point short period of time, and can also improve the distinctive stink of fecaluria.In addition, produce reaction heat, the temperature of mixture reaches 75 ℃～85 ℃, has almost killed the existing assorted bacterium that contains harmful bacterium such as pathogenic bacteria in the mixture.

The mixture of curing or spheroidizing is flowed to by worm conveyor 27 and carries with container 5, and this mixture is housed in the described container in right amount.The conveying of having accommodated mixture, is sling by lift (omitting diagram) movably along overhead guide rail after having accommodated the mixture of handling chicken manure as aftermentioned with container 5, is transported to fermentor tank 40.The mouth of casting of opening the bottom then can be with in the two mixtures input jar.

On the other hand, in chicken manure reaction machine 3, drop into an amount of chicken manure.When in chicken manure reaction machine 3, containing an amount of chicken manure, cooperate the wollastonite of supplying with by the worm conveyor 311 of wollastonite feedway 31 and mix stirring by predetermined proportion.

Moreover, in this mixture, mix by vitriol oil feedway 32 give pipe 321 vitriol oils that transport, in the stirred pot 33 of chicken manure reaction machine 3, stir and make it reaction.Utilize the reaction of this wollastonite and the vitriol oil, identical with the situation of above-mentioned pig manure or human excrement, mixture solidified or spheroidizing, stink also is improved, and utilizes reaction heat can kill assorted bacterium.

In addition, chicken manure is the chicken manure with respect to 100 weight parts with the ratio that cooperates of the wollastonite and the vitriol oil, and wollastonite is 9 weight parts, and the vitriol oil is 6 weight parts.

The processing of above-mentioned chicken manure makes hydro-cylinder 333 starts after finishing, and opens lid 35, takes out the mixture of curing or spheroidizing from conveying end 330, is housed in above-mentioned conveying with in the container 5.Carry with the mixture of processing pig manure of accommodating in the container 5 or human excrement and the blending ratio of handling the mixture of chicken manure to be, with respect to the mixture of the processing pig manure of 100 weight parts, the mixture of processing chicken manure is 20 weight parts.

Carry the fermentor tank 40 that is transported to fermentation unit 4 with container 5 by overhead driving (diagram is omitted).

In addition, the mixture of processing chicken manure is not necessarily non-sneaks in the mixture of handling pig manure in carrying with container 5, also can be delivered directly to fermentor tank 40 and also mix according to the above ratio.

Two kinds of mixture naturally cooling in the fermentor tank 40 when being cooled to the reproducible temperature of effective microbe, add an amount of effect microorganism.Then, mix by mobile whipping appts 41 and to stir, fermentation preset time and make it composting.In addition, because there is the assorted bacterium that contains harmful bacterium such as above-mentioned pathogenic bacteria in the mixture hardly, so the effective microbe that adds can fully activate.

In addition, by in the mixture of handling pig manure or human excrement according to the above ratio the mixture of combination treatment chicken manure ferment, just can under good order and condition, ferment and form the fine compost.

Though it is agnogenio, it is generally acknowledged that the chances are owing to the protein that contains in a large number in nitrogen that contains in a large number in the chicken manure or the chicken manure movable necessary energy of effective microbe that under vitriol oil effect, decomposed the amino acid supplementation that generates.

In addition, the inventor has tested the mixture of combination treatment chicken manure not and only added the situation that effective microbe ferments in the mixture of handling pig manure or human excrement, but not fermentation in four months duration of test.In contrast, mixed material just fermentation of the mixture of handling chicken manure since second day.

The compost that adopts the aforesaid method manufacturing is analyzed analytical results following (with reference to table 1):

Table 1

Material	Mark	Unit	No chicken manure primary treatment compost	There is chicken manure fermenting to handle compost
Material	Mark	Unit	No chicken manure primary treatment compost	There is chicken manure fermenting to handle compost	Arsenic	??As	Mg/kg does	??4.98	??0.62
Cadmium	??Cd	Mg/kg does	??0.1	??0.05	Arsenic	??As	Mg/kg does	??4.98	??0.62
Cadmium	??Cd	Mg/kg does	??0.1	??0.05	Total mercury	??T-Hg	Mg/kg does	??1.25	??0.03
Total nitrogen	??T-N	??％	??0.21	??2.03	Total mercury	??T-Hg	Mg/kg does	??1.25	??0.03
Total nitrogen	??T-N	??％	??0.21	??2.03	Total phosphorus	??P ₂O ₅	??％	??0.08	??3.87
Potassium	??K ₂O	??％	??0.02	??4.13	Total phosphorus	??P ₂O ₅	??％	??0.08	??3.87
Potassium	??K ₂O	??％	??0.02	??4.13	Calcium	??CaO	??％	??5.68	??13.00
Silica	??Si	??％	??10.40	??10.60	Calcium	??CaO	??％	??5.68	??13.00
Silica	??Si	??％	??10.40	??10.60	Carbon nitrogen ratio	??C/N		??17.10	??6.00
Moisture	??H ₂O	??％	??48.10	??46.40	Carbon nitrogen ratio	??C/N		??17.10	??6.00
Moisture	??H ₂O	??％	??48.10	??46.40	Hydrogen ion concentration	??pH		??1.60	??7.50

Embodiment

Compost with the aforesaid method manufacturing applies fertilizer on the spot, confirms arable farming is produced effect.

This method is as follows: at first guarantee everywhere experimental field, each be divided into respectively in experimental field do not apply fertilizer with fertilising ground, grow the same crop in various places.Cultivated following crop in experimental field at each: 1. barrel mandarin orange (Citrus that Taiwan originates in); 2. 3. sugarcane (two places) of Hylocereus undatus (dragon fruit).

Embodiment 1

Crop: bucket mandarin orange

Each tree at fertilising side fertilising 1kg, is observed the change procedure of tree.

Apply fertilizer after 50 days, the leaf of unmanured tree still turns to be yellow and the leaf total amount reduces.In addition, fruit diameter also has only about 4mm.

In contrast, the leaf of the tree of fertilising is green and the leaf amount is also many.Fruit diameter reaches about 8mm in addition.

Embodiment 2

Crop: Hylocereus undatus

Each tree at fertilising side fertilising 5kg, is observed the change procedure of tree.

Apply fertilizer after 120 days, the tree of fertilising and unmanured tree are gathered in the crops equally.The harvest yield of tree of fertilising is about 4 times of harvest yield of unmanured tree.In addition, compare with the product of unmanured tree, the product of the tree of fertilising is tasted and is obviously felt to have improved pol.

Embodiment 3

Crop: sugarcane

Per 10 ares of fertilising 600kg, the change procedure of observation sugarcane.

Apply fertilizer after 90 days, the about 180cm of the height of the sugarcane of not applying fertilizer, dried sturdy degree is about 3cm, the wide 4cm that is about of leaf.

In contrast to this, the fertilising sugarcane is 200～230cm, the dried about 4～4.5cm of sturdy degree, the wide 5.5cm that is about of leaf.

Embodiment 4

Crop: sugarcane

Experimental field: the Okinawa Prefecture name is protected the geographic poor and barren land in Tian Ren room, city

Per 10 ares of fertilising 3000kg, the change procedure of observation sugarcane.

After fertilising 180, the sugarcane of using organic compost in the past and the sugarcane of using compost of the present invention are adopted 10 strains respectively measured Brix and pol.And also calculated prediction harvest yield (with reference to table 2).

In addition, from fertility status, the sugarcane of using organic compost in the past is ripe, and the sugarcane of using compost of the present invention also is in the process of growth.It is generally acknowledged that results were suitable after 60 days.

Table 2

	Organic compost in the past	Compost of the present invention
	Organic compost in the past	Compost of the present invention	Rate of fertilizer application	??3000kg/10a	??3000kg/10a
Expectation harvest yield at that time	??6500kg	??16000kg	Rate of fertilizer application	??3000kg/10a	??3000kg/10a
Expectation harvest yield at that time	??6500kg	??16000kg	Expectation harvest yield during results	??7000kg	??20000kg
Brix at that time	??17	??23	Expectation harvest yield during results	??7000kg	??20000kg
Brix at that time	??17	??23	Expectation Brix during results	??17	??24
Pol at that time	??12.04％	??14.58％	Expectation Brix during results	??17	??24
Pol at that time	??12.04％	??14.58％	Pol during results	??12.04％	??15.00％

So-called Brix is meant the shared ratio of material (soluble solids composition) behind the piece of being dried to that is dissolved in the squeezeding juice, wherein except carbohydrates such as granulated sugar (sucrose) and glucose, also includes nutritive ingredients such as ash content or calcium.

(evaluation)

From the various embodiments described above as can be known: by using compost of the present invention in right amount, can improve the fertility of soil, plant growth is good, can breed the high-quality crop of pol height and so on.And can also increase the harvest yield of crop.

Term that uses in this specification sheets and expression are for thorough explanation the present invention rather than limitation of the invention, do not get rid of with above-mentioned term, express term, expression of equal value.In addition, the present invention is not limited to illustrated embodiment, can do various changes in the scope of technological thought.

The present invention has said structure, produces following effect:

(a),,, can also increase harvest yield so can cultivate the fine crop because can increase soil fertility according to compost of the present invention.

(b) according to the present invention, by in the mixture of handling pig manure or human excrement according to the above ratio the mixture of combination treatment chicken manure ferment, just can under good order and condition, ferment and make the fine compost effectively.

That is to say, be reflected at solid shapeization of fecaluria realization or the spheroidizing that makes water ratio high in the extremely short time by wollastonite and vitriolic, thereby stink is improved, even simultaneously aspect the big real standard of treatment capacity, also the fermentation that can carry out conscientiously based on effective microbe is a composting, for example use fecalurias such as pig manure urine or human excrement, the result can make compost effectively.

(c) fecaluria of the present invention reaction facility have worm conveyor, are used for carrying while stirring being mixed with the mixture that was stirred and the material of the vitriol oil; And the part of mixing the vitriol oil is arranged on the transfer base side of worm conveyor or leads to the giving in the passage of mixture of transfer base side.According to fecaluria reaction machine of the present invention, for mixing the vitriol oil, press equipressure, so device can be simplified because need hardly to inject.

(d) device of giving of the present invention is provided with a plurality of fecaluria whipping apptss at least, and supplies with wollastonite selectively to each fecaluria whipping appts, and the stink in the fecaluria whipping appts can outwards not leaked from supplying with part.According to the device of giving of the present invention, for example when a side fecaluria whipping appts carries out stir process etc., can be transported to the opposing party's fecaluria whipping appts to fecaluria and wollastonite to descend the preparation of subjob.Thus, can carry out the manufacturing of compost effectively.

Claims

1, a kind of compost, it is characterized in that: described compost obtains by following method: mix wollastonite in pig manure urine or human excrement, then mixes and react and make it curing or spheroidizing with the vitriol oil, in the material that obtains like this, be blended in and mix wollastonite in the chicken manure, then mix and make it to react and solidify or the material of spheroidizing with the vitriol oil, with described mixture is substratum, adds effective microbe and makes it fermentation.

2, a kind of manufacture method of compost, it is characterized in that: in pig manure urine or human excrement, mix wollastonite, then mixes and react and make it curing or spheroidizing with the vitriol oil, in the material that obtains like this, be blended in and mix wollastonite in the chicken manure, then mix and make it to react and solidify or the material of spheroidizing with the vitriol oil, with described mixture is substratum, adds effective microbe and makes it fermentation.

3, according to the manufacture method of the compost of claim 2 record, it is characterized in that: the wollastonite that in the pig manure of 100 weight parts urine or human excrement, mixes 10～25 weight parts, then mixes and react and make it curing or spheroidizing with the vitriol oil of 5～15 weight parts, in material 100 weight parts that obtain like this, be blended in mix in the chicken manure wollastonite, then mix with the vitriol oil and make it to react and solidify material 15 weight parts of spheroidizing or more than, with described mixture is substratum, adds effective microbe and makes it fermentation.

4, according to the manufacture method of compost of claim 2 or 3 records, it is characterized in that: add a kind of selecting among zinc, manganese, molybdenum, magnesium, copper, the iron, two or more.

5, a kind of manufacturing installation of compost is characterized in that, it has: the fecaluria feedway of supplying with pig manure urine or human excrement; Supply with the wollastonite feedway of wollastonite; Supply with the vitriol oil feedway of the vitriol oil; The pig manure urine supplied with or human excrement and wollastonite are mixed the fecaluria whipping appts that stirs; To mix the mixture that stirred by the fecaluria whipping appts and be mixed the fecaluria reaction machine that stirs and make it to react with the vitriol oil of being supplied with; Mix and stir chicken manure and wollastonite, and then in its mixture, mix the chicken manure reaction machine that stirs the vitriol oil and make it to react; The fermentation unit that in the mixture of the material that gets by fecaluria reaction machine and chicken manure reaction mechanism, adds effective microbe and make it to ferment.

6, according to the compost manufacturing installation of claim 5 record, it is characterized in that: fecaluria reaction facility have worm conveyor, are used for carrying while stirring the mixture that is mixed with mixed stirring and the material of the vitriol oil; And the part of mixing the vitriol oil is arranged on the transfer base side of worm conveyor or leads to the giving in the passage of mixture of transfer base side.

7, according to claim 5 or the 6 compost manufacturing installations of putting down in writing, it is characterized in that: the wollastonite feedway has the device of giving, describedly give device and be provided with a plurality of fecaluria whipping apptss at least and be connected, and supply with wollastonite selectively to each fecaluria whipping appts, the stink in the fecaluria whipping appts can outwards not leaked from supplying with part.