JP2019130434A - Manufacturing method of fulvic acid polysilica iron solution - Google Patents

Abstract

To provide a manufacturing method of a fulvic acid polysilica iron solution capable of efficiently manufacturing fulvic acid iron in a short time.SOLUTION: A manufacturing method of a fulvic acid polysilica iron solution comprises a process of preparing a processing device 10 having a closed vessel 12 having a closable treatment space on the inside, steam jetting means 14 for jetting high temperature-high pressure steam, a supply part for supplying a raw material and a discharge part 16 for discharging a processing liquid to an external part, a raw material input process of inputting a woody material and/or a grass material and polysilica iron from the supply part in the treatment space of the closed vessel 12, a processing process of providing a mixed solution including fulvic acid polysilica iron by subcritical water reaction treating while agitating a raw material by introducing steam of 2-35 atm in pressure at 120-250°C in the temperature of the woody material and steam of 2-25 atm in pressure at 100-200°C of the grass material and a process of providing a fulvic acid polysilica iron solution by separating fulvic acid polysilica iron from the mixed solution.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a method for producing a fulvic acid polysilica iron solution.

  In the natural world, fulvic acid is produced in humic substances formed by humming plant leaves and stems. Then, this fulvic acid is combined with iron dissolved in water in an oxygen-free state in the soil, and iron fulvic acid is generated. This fulvic acid iron is transported to the sea by rivers and contributes to the growth of phytoplankton and seaweed. In recent years, it has been reported that the iron fulvic acid can prevent the burning of the sea, decompose the sediment on the seabed, and purify the river.

In addition, fulvic acid is combined with silicic acid and transported from rivers to the sea. Among sea phytoplankton, diatoms play an important role in the food chain, but diatoms require silicon for growth. In order to efficiently supply silicon, fulvic acid polysilica iron combined with silicic acid in addition to iron fulvic acid is optimal.

  As described above, in the natural world, the encounter between fulvic acid and iron, and fulvic acid and silica are governed by chance, and in the production methods described in Patent Documents 1 and 2, the production amount of fulvic acid iron is unknown. Therefore, it is difficult to control the production amount, and it is impossible to stably supply iron fulvic acid-containing substances and iron fulvic acid, and the problem of high manufacturing cost cannot be solved.

  Therefore, in Patent Document 3, a method for producing an iron fulvic acid-containing material is proposed in order to solve the above-described conventional problems, and the proposed method for producing an iron fulvic acid-containing material is used for fermentation / sterilization of organic waste. A liquid substance composed of silica iron is mixed and aged in a fermented processed product in which fulvic acid is generated by the treatment.

According to this manufacturing method, a liquid substance composed of polysilica iron is mixed with fermented and sterilized organic waste, and the fulvic acid and silica iron-based material produced in the fermentation and sterilization process of organic waste during the aging process are mixed. By chelating with an iron component, there is a possibility that a fulvic acid polysilica iron material containing water-soluble silica can be produced stably and inexpensively.
By the way, although there is a warning due to the lack of silica in the natural world, a useful substance, iron iron or fulvic acid silica, exists only in the natural world, and a new method for producing it has not yet been established.
The object of the production method of Patent Document 3 is a fulvic acid polysilica iron material containing water-soluble polysilica, and not the produced fulvic acid polysilica iron.

JP 2005-34140 A Japanese Patent No. 4710036 No. 2014-38596

  Then, this invention aims at providing the manufacturing method of the fulvic acid polysilica iron which can manufacture fulvic acid polysilica iron efficiently in a short time.

The above object can be achieved by the workpiece transfer apparatus according to the present invention having the following structures (1) to (24).
(1)
A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
A raw material charging step of charging a raw material mainly composed of wood material and polysilica iron from the supply unit into the processing space of the closed container of the processing device,
Steam having a temperature of 120 to 250 ° C. and a pressure of 5 to 35 atm is introduced into the processing space in which the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A treatment step to obtain a mixed solution containing acid polysilica iron, and
A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution by separating fulvic acid polysilica iron from the obtained mixed solution to obtain a fulvic acid polysilica iron solution.
(2)
A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
A raw material charging step of charging a raw material mainly composed of wood material and polysilica iron from the supply unit into the processing space of the closed container of the processing device,
Steam having a temperature of 120 to 250 ° C. and a pressure of 5 to 35 atm is introduced into the processing space in which the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A mixed solution containing acid polysilica iron and a treatment step for obtaining a solid residue remaining in the mixed solution;
The solid residue obtained in the pretreatment step is separated from the mixed solution, the solid residue obtaining step for obtaining the solid residue, and the fulvic acid polysilica iron is separated from the mixed solution from which the solid residue is separated, A fulvic acid polysilica iron solution obtaining step for obtaining a fulvic acid polysilica iron solution is provided.
(3)
The method for producing a fulvic acid polysilica iron solution according to the above (1) or (2), wherein the wood is felled wood or waste wood.
(4)
(3) The method for producing a fulvic acid polysilica iron solution according to (3) above, wherein the felled material is made of hardwood or softwood.
(5)
(4) The method for producing a fulvic acid fulvic acid polysilica iron solution according to (4) above, wherein the broad-leaved tree is white birch, willow, chestnut, oak or beech.
(6)
(4) The method for producing a fulvic acid polysilica iron solution according to (4) above, wherein the conifer is pine, cedar, hinoki or tomato.
(7)
The method for producing a fulvic acid polysilica iron solution according to (3), wherein the waste material is a solid material or a plywood material.
(8)
The method for producing a fulvic acid polysilica iron solution according to any one of (1) to (7), wherein the treatment step is performed for 30 minutes to 12 hours.
(9)
The method for producing a fulvic acid polysilica iron solution according to (3), wherein the main raw material is hardwood and the pressure of the steam introduced in the treatment step is 5 to 25 atm.
(10)
The method for producing a fulvic acid polysilica iron solution according to (3), wherein the main raw material is conifer and the pressure of the steam introduced in the treatment step is 20 to 35 atm.
(11)
A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
Into the processing space of the closed container of the processing apparatus, a raw material charging step of charging a raw material mainly composed of herbaceous material made of gramineous plants and polysilica iron from the supply unit,
While introducing the steam at a temperature of 100 to 200 ° C. and a pressure of 2 to 25 atm into the treatment space into which the raw material has been charged, the raw material is subjected to a subcritical water reaction treatment while stirring the raw material, A treatment step to obtain a mixed solution containing fulvic acid polysilica iron, and
A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution by separating fulvic acid polysilica iron from the obtained mixed solution to obtain a fulvic acid polysilica iron solution.
(12)
A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
Into the processing space of the closed container of the processing apparatus, a raw material charging step of charging a raw material mainly composed of herbaceous material made of gramineous plants and polysilica iron from the supply unit,
Steam having a temperature of 100 to 200 ° C. and a pressure of 5 to 25 atm is introduced into the treatment space where the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A mixed solution containing acid polysilica iron and a treatment step for obtaining a solid residue remaining in the mixed solution;
The solid residue obtained in the pretreatment step is separated from the mixed solution, and the fulvic acid polysilica iron is separated from the solid residue obtaining step and the mixed solution from which the solid residue has been separated to obtain a fulvic acid silica iron solution. A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution.
(13)
The method for producing a fulvic acid polysilica iron solution according to (11) or (12), wherein the herbaceous material is a felling or cutting material or a waste material.
(14)
The harvested or harvested material is any one of rice, wheat, barley, oats, rye, millet, millet, millet, sorghum, sorghum, bamboo shoot, sugar cane, pearl barley, reed, suki, sasa, danchiku, shiroganeyoshi and shiba. (13) The method for producing a fulvic acid polysilica iron solution according to the above (13).
(15)
The method for producing a fulvic acid polysilica iron solution according to (14), wherein the felling or cutting material is rice straw or wheat straw.
(16)
(15) The method for producing a fulvic acid polysilica iron solution according to (15), wherein the felling or cutting material is bamboo.
(17)
The method for producing a fulvic acid polysilica iron solution according to (16), wherein the bamboo material is in a chip shape.
(18)
The manufacturing method of the fulvic acid polysilica iron solution of said (11) whose raw material is a used waste material.
(19)
(18) The method for producing a fulvic acid polysilica iron solution according to (18), wherein the waste material is an old tatami floor.
(20)
The method for producing a fulvic acid polysilica iron solution according to any one of (11) to (19), wherein the treatment step is performed for 30 minutes to 12 hours.
(21)
The method for producing a fulvic acid polysilica iron solution according to any one of (1) to (20), wherein the raw material is introduced in a volume ratio of 90% or less of the treatment space.
(22)
The method for producing a fulvic acid polysilica iron solution according to any one of (1) to (20), wherein the raw material is introduced in an amount of 50 to 80% by volume.
(23)
The method for producing a fulvic acid polysilica iron solution according to any one of (1) to (22), wherein the stirring in the processing step is performed by a rotating stirring member arranged in the processing space.
(24)
The method for producing a fulvic acid polysilica iron solution according to any one of (1) to (23), wherein an alkaline solution is added as an additive in the raw material charging step.

  The present invention provides for the first time a method for producing fulvic acid polysilica iron, and according to the present method, the production process of fulvic acid polysilica iron does not require time-consuming processes such as fermentation and aging. The fulvic acid polysilica iron can be produced stably in an extremely short time.

It is sectional drawing which shows an example of the manufacturing apparatus for enforcing the manufacturing method of the fulvic acid polysilica iron solution by embodiment of this invention.

Hereinafter, an embodiment of a method for producing a fulvic acid polysilica iron solution of the present invention will be described.
First, an example of the manufacturing apparatus (processing apparatus) 10 for implementing the manufacturing method of the fulvic acid polysilica iron solution by embodiment of this invention is demonstrated.
FIG. 1 is a sectional view of the manufacturing apparatus.

  The manufacturing apparatus 10 includes a sealed container 12 having a closed space S1 that accommodates a raw material that is a broken material of a wood material or a plant belonging to the family Gramineae, and a high-temperature and high-pressure that is subcritical water in the sealed container 12. The steam jetting means 14 for jetting steam, the discharge port 16 provided on the bottom side of the sealed container 12 and having an opening / closing mechanism 26, and the raw material and liquid processed only by direct discharge operation from the discharge port 16 are separated. And a separation and recovery means 18 for recovery. The shape of the airtight container 12 may be, for example, a rectangular box shape, a three-dimensional polygonal cylinder shape, a cylindrical shape, a barrel shape, a drum shape, or any other arbitrary shape, but using gravity from the discharge port 16 provided on the lower surface side. A shape that is discharged is preferred. It is preferable that the bottom surface of the sealed container is provided with a downward slope toward the discharge port.

  The separation / recovery means 18 has another closed space S2 different from the closed space S1 of the sealed container 12, a liquid recovery unit 50 communicating with the inside of the sealed container 12 through the discharge port 16, and the inside of the sealed container 12 It is good also as having the natural flow collection | recovery mechanism 52 which collects only the liquid of this to the collection | recovery part 50 by natural flow through the discharge port 16. The raw material as solid content processed in the vicinity of the discharge port 16 remains in the sealed container 12 as it is, and only the liquid naturally flows down to the recovery unit 50 using gravity, whereby the raw material and the liquid can be separated and recovered. The configuration of the recovery unit 50 may be arbitrary as long as it has a closed space S2 for recovering liquid, such as a metal tank, a three-dimensional polygonal box, or a tubular body. A plurality of accommodating portions may be formed.

The natural flow recovery mechanism 52 may include the same pressure forming means 62 that makes the closed space S1 of the sealed container 12 and the closed space S1 of the recovery unit 50 have the same pressure before the liquid recovery operation. If the sealed container 12 and the recovery unit 50 are configured to always have the same pressure, the liquid recovery operation can be performed immediately after the processing, and the operation time can be shortened.
In the above example, the example in which the separation means is incorporated in the processing apparatus has been described. However, the processing apparatus itself may be provided separately without providing the separation means.

  Moreover, you may provide the same pressure formation means 62 for making the closed space S1 of the said airtight container 12 and the closed space S2 of the collection | recovery part 50 into the same pressure. The same-pressure forming means 62 has a same-pressure communication pipe 64 that communicates the closed space S1 of the sealed container 12 and the closed space S2 of the recovery unit 50 through another path different from the liquid recovery path via the discharge port 16. It is good as well. The same pressure communication pipe 64 may be in constant communication with the closed space S1 and the closed space S2 so that the inside of the sealed container 12 and the collection unit 50 are always at the same pressure. The same-pressure communication pipe 64 may be at the same pressure by communicating the closed container 12 and the recovery unit 50 at least before the liquid recovery operation, and an open / close mechanism for connecting and blocking the same-pressure communication pipe. It may be provided.

  Further, the communication between the same-pressure communication pipe 64 forming another path and the sealed container 50 may be performed via a communication connection portion 68 set on the upper end side of the sealed container 12.

  The natural flow recovery mechanism 52 includes a liquid recovery channel 54 that connects the discharge port 16 of the sealed container 12 and the recovery unit 50 in communication, and the liquid recovery channel 54 is connected to the recovery unit from the communication side with the discharge port 16. It may be provided horizontally or downwardly inclined toward the 50 side.

  In addition, an opening / closing mechanism 26 is provided in the middle of the discharge path R1 from the processed raw material discharge port 16, and the liquid introduction port 58 of the liquid recovery passage 54 is connected to the discharge upstream side of the opening / closing mechanism 26. It is good.

  In addition, the liquid recovery channel 54 is selected so that the channel is shut off during processing of the raw material in the sealed container 12 and the channel is connected when only the liquid is recovered after the processing. An opening / closing mechanism 60 for switching between the two may be provided.

  In addition, the bottom surface of the closed space S <b> 2 of the collection unit 50 may be provided lower than the position of the discharge port 16 of the sealed container 12.

  The recovery unit 50 may be provided such that the liquid level WL of the liquid recovered in the closed space S2 is always lower than the discharge port 16.

  It is good also as having the stirring means 30 which stirs a raw material in the airtight container 12. FIG.

  Further, the sealed container 12 is formed in a side-down barrel shape in which the discharge port 16 is provided on the bottom side of the left and right center part, and the diameter is gradually reduced from the left and right center part toward both left and right sides. Includes a rotating shaft 49 that is provided horizontally in the sealed container 12 and rotatably supported, and a stirring blade 48 that is attached to the rotating shaft 49 and has a portion that extends in the circumferential direction of the rotating shaft 49. The length from the rotating shaft 49 of the stirring blade 48 to the tip of the blade is long at the central position in the longitudinal direction of the rotating shaft 49 corresponding to the sideways barrel shape of the sealed container 12, and gradually decreases toward both ends. It is good also as having been formed.

  Further, the steam jetting means 14 includes a rotary shaft / steam jet pipe 28 constituted by forming the rotary shaft 49 as a hollow tube and forming a plurality of steam jet holes 44 on the peripheral surface of the hollow tube. Also good.

In this example, the sealed container 12 is supported by the support legs 13 so as to be arranged at a certain height from the ground. The sealed container 12 is formed in a side-down barrel shape whose diameter is gradually reduced from the central portion in the left-right direction toward the end walls 12a on the left and right ends. The sealed container 12 is formed, for example, by processing a metal plate so as to have heat and pressure resistance, and is provided with a size that can accommodate about 2 m ^{3 of} raw materials. The closed container 12 is provided with an input part 20 above the center part and a discharge part 22 at the bottom side of the center part, and is provided to be opened and closed by opening / closing mechanisms 24 and 26, respectively. In the closed space S <b> 1 of the hermetic container 12, a steam ejection pipe 28 constituting the steam ejection means 14 and a stirring means 30 for stirring the raw material are disposed. The sealed container 12 is provided with a safety valve 32 that can release the internal steam when the internal pressure becomes higher than a set value, for example, the set pressure can be adjusted. Further, a silencer / deodorizer 34 is provided in the middle of the exhaust pipe connected to the safety valve 32, and the steam exhausted through the safety valve 32 is silenced and deodorized and discharged to the outside air side. .

  As shown in the figure, the discharge port 16 is opened on the bottom side of the central portion in the left-right direction of the sealed container 12 and is provided with the raw material discharge direction downward. The diameter of the discharge port 16 is, for example, about 300 mm. The discharge port 16 is connected to a discharge tube 36 projecting downward to form a discharge path R1 for processed raw material, and is provided in the middle of the discharge path R1 to open and close the discharge port 16. An opening / closing mechanism 26 is provided. That is, the discharge unit 22 includes a discharge port 16, a discharge tube 36, and an opening / closing mechanism 26. Since the sealed container 12 is laid sideways and formed into a barrel shape, the raw materials inside easily gather toward the center where the discharge port 16 is provided due to gravity, and the material can be easily discharged just by opening the opening / closing mechanism 26. 16 can be discharged.

  An input port 42 is opened on the upper side of the closed container 12 in the input unit 20, and an input tube 43 protruding upward is attached to the input port 42, for example, a ball so as to open and close the inside of the input tube 43. An opening / closing mechanism 24 such as a valve is provided. Through the opening / closing mechanism 24, the inlet 42 can be opened and the raw material can be charged into the sealed container, and is closed during processing to keep the closed space S1 in the sealed container 12 closed.

  The steam ejecting means 14 ejects high-temperature and high-pressure steam into the sealed container 12, puts the inside of the sealed container 12 into a high-temperature and high-pressure state, and processes the raw material through the steam. As shown in FIG. 1, the steam ejection means 14 includes a steam ejection pipe 28 formed of a hollow pipe disposed in the hermetic container 12 and formed with a large number of steam ejection holes 44 on the peripheral surface side, and steam generation such as a boiler. And a steam feed pipe 47 for supplying steam from the steam generator 46 into the steam jet pipe 28. The steam ejected from the steam ejecting means 14 into the sealed container 12 is set to a high temperature and high pressure such as subcritical water in order to properly process the raw material. For example, the steam ejected from the steam ejection pipe 28 is set to a temperature of 100 to 250 ° C. and a pressure of about 5 to 35 atm. And the inside of the airtight container 12 is made into the temperature of 100-250 degreeC, and the pressure of about 5-35 atm. The steam ejection pipe 28 is long in the horizontal direction at a substantially central position in the vertical direction of the sealed container 12 and is rotatably supported via bearings 45 provided on both end walls 12a of the sealed container. That is, the steam ejection pipe 28 is configured to directly apply the steam to the raw material while ejecting the steam radially while rotating around the horizontal axis. Note that the steam ejection pipe 28 is rotated by obtaining a rotational driving force from a rotational driving device 51 such as a motor via a chain or the like. Further, the steam jet pipe 28 is provided with a stirring blade 48 constituting a stirring means, and the steam jet pipe 28 also serves as the rotating shaft 49 of the stirring means. That is, in the present embodiment, the steam jetting means 14 is a rotating shaft / steam that is configured by forming the rotating shaft 49 of the stirring means as a hollow tube and forming a plurality of steam jetting holes on the peripheral surface of the hollow tube. A jet pipe 28 is included. Note that the steam ejection means is not limited to this configuration, and may be any other configuration such as a configuration for ejecting steam from the tip of a tube inserted into a sealed container, a configuration in which a plurality of steam ejection tubes are arranged, and the like. Good.

  The stirring means 30 is a means for stirring the raw material to be processed in the sealed container, and can process the raw material at an early stage without unevenness. The stirring means 30 includes a rotating shaft 49 composed of the steam ejection pipe 28 and a stirring blade 48 attached to the rotating shaft 49 and having a portion extending in the circumferential direction of the rotating shaft. In the present embodiment, the stirring blade 48 is formed of a right-handed spiral blade 48a and a left-handed spiral blade 48b that are provided in a reversely wound manner at approximately the center position in the axial direction of the rotating shaft 49. The stirring blade 48 is provided such that the length from the rotating shaft to the blade tip is gradually reduced from the left and right central portions toward both ends. Thereby, a raw material can be reliably stirred corresponding to the sideways barrel shape of the airtight container 12. Furthermore, a certain gap H is provided between the blade tip and the inner wall of the sealed container 12. The spiral blades 48a and 48b agitate the raw material while crushing the solid raw material while conveying the raw material from the central part toward the both end walls. The raw material conveyed to the both end walls 12a side by the stirring blade 48 is pushed by the raw material conveyed later on the end wall 12a side so as to return to the center through the gap H along the inner wall of the hermetic container 12. It is conveyed to. The stirring means 30 is not limited to the above configuration, and may have any other configuration.

  The separation / recovery means 18 is a separation / recovery means for separating and recovering the processed raw material and the liquid in the sealed container 12 after the steam treatment only by direct operation from the discharge port. As shown in FIG. 1, the separation / recovery means 18 collects the liquid recovery unit 50 communicating with the inside of the sealed container 12 through the discharge port 16 and the recovery unit 50 by natural flow through the discharge port 16. And a natural flow recovery mechanism 52.

  The collection unit 50 is a second closed container having inside another closed space S2 different from the closed space S1 of the closed container 12. The collection unit 50 is made of, for example, a metal cylindrical sealed tank having heat and pressure resistance. The collection unit 50 is connected to the discharge port 16 of the sealed container 12 through a liquid collection channel 54 formed of, for example, a metal pipe member. The recovery unit 50 is provided such that the bottom surface of the closed space S <b> 2 is lower than the position of the discharge port 16 of the sealed container 12, and the liquid level WL of the liquid recovered in the closed space S <b> 2 is always lower than the discharge port 16. So that the liquid on the discharge port side can easily flow naturally to the collection unit side. The recovery unit 50 is provided with a recovered liquid extraction drain 56 that is opened and closed by an on-off valve.

  The natural flow recovery mechanism 52 is natural flow recovery means that causes only the liquid to flow from the discharge port to the recovery unit 50 by natural flow due to the gravity of the liquid accumulated in the sealed container 12. The natural flow recovery mechanism 52 is configured to include a liquid recovery flow path 54, and the liquid recovery flow path 54 is branched from the discharge path R 1 of the processed raw material by connecting the liquid introduction port 58 to the discharge port 16. A liquid recovery path R2 is formed. In the present embodiment, the liquid recovery channel 54 is provided by a metal pipe having an inner diameter of about 6 mm, for example. The liquid recovery channel 54 is provided with an opening / closing mechanism 60 that selectively switches the communication state of the channel. The opening / closing mechanism 60 is switched so as to shut off the flow path during processing of the raw material in the hermetic container and to connect the flow path when only the liquid is separated and recovered after the processing. As a result, the liquid in a state containing moisture and vapor contained in the raw material at the same time as the raw material and containing bacteria, malodorous components and the like in the raw material can be treated with high-temperature and high-pressure steam. And the liquid that is separated and recovered after the treatment can be recovered in a state of sterilization, decomposition of malodorous and harmful components, etc., it is not necessary to perform the secondary treatment of the separated and recovered liquid, and labor is not required, Time can be reduced.

  In the liquid recovery channel 54, the liquid inlet 58 is connected in communication with a position upstream of the opening / closing mechanism 26. Therefore, with the opening / closing mechanism 26 of the discharge port 16 closed, the opening / closing mechanism 60 of the liquid recovery channel 54 is opened to bring the channel into a communication state, whereby the liquid is separated and recovered from the discharge port. The liquid recovery flow path 54 is connected in a direction orthogonal to the discharge cylinder 36, and a liquid recovery path R2 is provided in a direction orthogonal to the raw material discharge path R1. That is, in the closed state of the opening / closing mechanism 26, the liquid flows in a direction crossing the direction in which the deposition pressure of the raw material in the sealed container is applied. Thereby, it becomes a structure with a simple structure and it is hard to enter a raw material into the liquid inlet 58, and only a liquid can be naturally flowed down to the liquid collection | recovery path 54, and a liquid can be separated and collected favorably. It should be noted that if the momentum in which the liquid in the sealed container 12 flows to the liquid inlet 56 is too strong, the raw materials may flow together due to the force of the liquid flow. Therefore, the processed raw materials are preferably not carried away. The connection configuration such as the liquid recovery path and the liquid inlet is set so that the flow is moderate. The liquid recovery channel 54 is provided horizontally horizontally from the communication side (liquid inlet side) to the discharge port 16 toward the recovery unit. Thereby, the flow of the liquid in the liquid recovery channel is smoothly performed, and the liquid flows naturally from the discharge port to the recovery unit. The liquid recovery channel 54 may be provided in a downwardly inclined manner toward the recovery unit so that the liquid flows more smoothly in the liquid recovery channel 54. At this time, for example, the liquid inlet 58 side may be provided horizontally up to a certain length and then provided with a downward slope. The liquid inlet 58 may be provided with a filter or the like as necessary.

  Further, as shown in FIG. 1, the natural flow mechanism 52 includes the same pressure forming means 62 that forms the closed space S <b> 1 of the sealed container 12 and the closed space S <b> 2 of the recovery unit 50 at the same pressure before the liquid recovery operation. Including. Normally, since the inside of the sealed container 12 after processing is at a high pressure, in the liquid recovery flow path, a pumping force due to a pressure difference acts toward the closed space S2 of the recovery unit having a lower pressure than in the sealed container. When such a pumping force is applied, both the liquid and the raw material flow into the liquid recovery flow path 54, making it difficult to separate and recover the liquid and the raw material, and the possibility that the raw material is clogged in the liquid recovery flow path is high. . By making the two closed spaces S1 and S2 of the closed container 12 and the recovery part 50 have the same pressure before the liquid recovery operation by the same pressure forming means 62, the difference in air pressure between the two closed spaces S1 and S2 is achieved. Can be prevented from being pumped, and can be successfully recovered in the recovery section while being separated from the raw material by utilizing the natural flow action of the liquid. Moreover, since the separation and recovery operation can be performed even in a high-pressure state in the sealed container after processing, the operation time can be shortened.

  The same-pressure forming means 62 establishes the closed space S1 of the sealed container 12 and the closed space S2 of the recovery unit 50 through another path R3 different from the liquid recovery path R2 (liquid recovery flow path 54) via the discharge port 16. The same pressure communication pipe 64 to be communicated is included. The same pressure communication pipe 64 is made of, for example, a metal pipe, and has a simple structure and can efficiently make the two closed spaces S1 and S2 have the same pressure. In FIG. 1, one end side of the same-pressure communication pipe 64 is connected to the upper end side of the left and right central part of the sealed container 12, and the other end side is connected to the upper end side of the recovery part 50. The communication between the same-pressure communication pipe 64 that forms another path R3 and the sealed container 12 is performed via a communication connection portion 68 set on the upper end side of the sealed container 12. The connection port of the communication connection portion 68 with the sealed container is set downward. Thereby, the raw material accumulated in the closed container 12 in the same pressure communication pipe 64 is difficult to enter the pipe, the raw material is prevented from clogging in the pipe, and the communication state of the same pressure communication pipe is maintained. The airtight container 12 and the collection | recovery part 50 can be made into the same pressure reliably. The same pressure communication pipe 64 is always in a communication state, and when the opening / closing mechanism 60 of the liquid recovery channel 54 is closed, the inside of the sealed container 12, the recovery unit 50, and the liquid recovery channel 54 are in the same pressure state. Become. Thereby, it is possible to prevent the raw material from being pumped due to a pressure difference on the liquid inlet 58 side of the discharge port 16 immediately after opening the opening / closing mechanism 60 of the liquid recovery channel 54. Further, even when the opening / closing mechanism 60 is opened to collect the liquid, the inside of the sealed container 12 and the inside of the collection unit 50 are always kept at the same pressure. Therefore, the same pressure state is maintained from before collection to after completion of collection, and only the liquid can be separated and collected by naturally flowing down from the discharge port 16 satisfactorily. Note that the same pressure forming means 62 is not limited to this configuration, and may have any configuration. For example, the same pressure forming means 62 is provided with another high pressure forming device that makes the inside of the recovery unit high pressure, and adjusts the pressure in the recovery unit while monitoring the pressure in the closed container with a sensor, so Pressure may be applied. Further, the inside of the sealed container may be decompressed.

Next, the manufacturing method of the fulvic acid iron solution by embodiment of this invention using the manufacturing apparatus 10 demonstrated above is demonstrated.
A method for producing a fulvic acid polysilica iron solution according to an embodiment of the present invention includes:
An apparatus preparation step for preparing the processing apparatus as described above;
A raw material charging step for charging a raw material mainly composed of woody material and / or gramineous plant and polysilica iron into the processing space of the closed container of the processing device,
When the raw material is wood material, the temperature is 120 to 250 ° C., the pressure is 12 to 35 atm (12 to 25 atm for hardwood, 20 to 35 atm for conifer), and the temperature is herb for the raw material. A vapor having a pressure of 5 to 25 atm at 100 to 200 ° C. is introduced into the processing space in which the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material to obtain a fulvic acid polysilica. Processing steps to obtain a mixed solution containing iron, and
A fulvic acid polysilica iron solution obtaining step of separating the fulvic acid polysilica iron from the obtained mixed solution to obtain a fulvic acid polysilica iron solution is provided.

Hereinafter, each process described above will be described in detail.
<< Device preparation process >>
A manufacturing apparatus (processing apparatus) as described above is prepared with reference to the drawings.

<Raw material input process>
Wood material as main material Chips made by breaking wood material (trunks, branches, leaves, etc.) can be used as the main material. The chip size is preferably about 5 to 150 cm for the long side and about 5 cm for the short side 2.
As the wood, generally, felled wood or waste wood can be used.
The logging material may be either broad-leaved trees or coniferous trees.
As the broad-leaved tree, any broad-leaved tree may be used, but at present, for example, birch, willow, chestnut, oak or beech can be preferably used.
At present, for example, pine, cedar, cypress or asunaro can be preferably used as the conifer.
When using felled timber, it is not necessary to remove the skin.

Examples of the waste material include wood waste (corner, plate material: solid material, bonded material / plywood material (plywood)) generated during the dismantling of a wooden building house. Such wood chips are usually used as chips and can be used as raw materials.
The above raw materials may be mixed and used. For example, when logging is performed in a normal household, various types of felled timber are discharged. These may be used as raw materials by mixing them as they are without sorting. Of course, waste chip may be mixed therein.

A herbaceous material made of a grass family plant as the main material A herbaceous material made of a grass family plant (stem (spear), branch, leaf, etc.) can be used as a main material. The length of the breakable material is preferably 400 mm or less, particularly 50 mm to 200 mm. If it is longer than the above range, it will be difficult to put it into the processing space, or it will become entangled with the stirring member, resulting in a decrease in production capacity. Even if the length is less than the above range, there is no problem in the production process of iron fulvic acid, but it takes time to break.

  The herbaceous material may be an old material such as a tatami floor.

  Rice plants include rice, wheat, barley, oats, rye, millet, millet, millet, sorghum, sorghum, bamboo, macomo, sugar cane, pearl barley, reed, susuki, sasa, danchiku, shiroganeyoshi, shiba, etc. Can be mentioned.

  About the plant main raw material demonstrated above, it can mix and use. The mixing ratio may be arbitrary.

Silica iron Polysilica iron as the main raw material is used in the form of a solution. In order to prevent the oxidation of polysilica iron from proceeding, it is important that the oxygen in the steam injected into the sealed container is removed in advance. In general, high temperature steam has been found to release oxygen.

The Fukuzai or additives <br/> secondary timber or additives, in order to efficiently generate more fulvic acid polysilica iron, it can be added alkanoate solution. The pressure and temperature of the vapor when adding the alkaline solution may be the same as when not adding.

The main raw material which is the grass or the wood material which is the chip or the rupture material as described above is put into the processing space, and the amount of the main raw material is 90% or less of the closed space S1 of the sealed container 12, that is, the processing space. In particular, it is preferably 50 to 80%. When the input amount of the raw material is lower than this range, the processing efficiency is poor, and when it exceeds, the steam cannot act well on the raw material, and there is a possibility that the production of polysilica fulvic acid iron is not sufficient.
Further, when the raw material input, is to introduce polysilicato iron is another main raw material in the form of a solution, sufficiently put polysilica iron as 10~30kg about (reaction processing space volume 2m ^3. For example Naoji Pharmaceutical Co., Ltd When the iron-based inorganic flocculant PSI-100 is used, it is desirable to add it (since the silica / iron ratio is 1.0%).

《Processing process》
In this step, steam is introduced into the processing space in which the raw material is charged. In the case of wood material and silica iron, this steam has a temperature of 120 to 250 ° C. and a pressure of 12 to 35 atm (for hardwood: 12 to 25 atm, for conifer: 20 to 35 atm). In this case, the temperature is 100 to 200 ° C. and the pressure is 5 to 25 atm. In the case of mixing, the temperature and pressure are taken into account according to the mixing ratio. The amount of steam introduced depends on the volume of the processing space and the amount of raw material to be processed, but is an amount that completely fills the surplus space (the space obtained by subtracting the volume of the raw material charged from the processing space). Is preferred.

In this processing step, as described above, the raw material is stirred while introducing steam into the processing space into which the raw material has been charged, and the raw material is processed by subcritical water reaction.
The treatment process time is preferably 30 minutes to 12 hours when the raw materials are wood material and silica iron, and 30 to 10 hours when the raw material is herb material. When the treatment time is shorter than the above range, the reaction time is not sufficient, that is, the production of fulvic acid is small, and the production of fulvic acid polysilica iron is not sufficient. When the above time range is exceeded, the fulvic acid changes to humic acid and the amount of fulvic acid polysilica iron is reduced, or the raw wood and herb are carbonized.

  The temperature in the treatment space in this treatment step varies depending on the type and state of the raw material used, but in the case of wood material and silica iron, the temperature is 120 to 250 ° C. and the pressure is 12 to 35 atm. In the case of herbaceous material and polysilica iron, the temperature is 100 to 200 ° C. and the pressure is maintained at 2 to 25 atm.

In this treatment step, the raw material is subjected to a subcritical water reaction treatment, and fulvic acid, fulvic acid polysilica iron, humic acid, and polymerized silicic acid are contained in the solution. This solution is a mixed solution containing fulvic acid, polysilica iron fulvic acid, and humic acid, and a mixed solution containing a suspension of wood or plant wood / and fragments thereof and a precipitate of polymerized silica. .

  In the mixed solution obtained in this step, among the total amount of fulvic acid polysilica iron and humic acid (in the solid content), fulvic acid polysilica iron is 3 to 12 in total when one of the main raw materials is woody material. %, In the case of herb wood, 2 to 10% is included.

《Cooling process》
A cooling step may be performed after the treatment step. In this cooling step, the inside of the treatment space is cooled, that is, the steam is cooled to obtain a solution containing fulvic acid, fulvic acid polysilica iron, and humic acid. This cooling is usually performed by natural cooling.

《Fulvic acid polysilica iron solution acquisition process》
In this step, first, the solution is separated from the solid. This separation is performed, for example, by allowing the solution component to fall naturally and leaving the solid component in the sealed container. This residual solid is a wood chip or the like to which polymerized silica adheres. On the other hand, humic acid, fulvic acid polysilica iron and fulvic acid are separated from the separated mixed solution to obtain a fulvic acid polysilica iron solution.
In the method for separating humic acid and fulvic acid polysilica iron in the solution obtaining step of the fulvic acid polysilica iron, the solution is acidified to pH, the humic acid is precipitated and separated, and the liquid is filtered. The pH of the solution is preferably 2 to 3.

[Example]
First, a processing apparatus having a structure as shown in FIG. 1 in which the volume of the processing space in the sealed container is 2 m ³ was prepared.
In the treatment space, white timber cutting chips and silica iron solution (Example 1), and willow cutting chips and polysilica iron solution (Example 2) were used as raw materials, respectively. went.
The average length of the wood material was about 10 cm in both long sides.
The input amount of the wood chip was the same for both, and was 1.6 m ³ (80% of the volume of the processing space). The amount of the polysilica iron solution input was the same for both, and was 1 kg.

After the introduction of these raw materials, a subcritical water reaction treatment was performed with the raw material steam by stirring with stirring means while introducing steam having a temperature of 200 ° C. and a pressure of 20 atm into the treatment space. The treatment time was 1 hour for both raw materials.
The state in the processing space in this processing step was a temperature of 200 ° C. and a pressure of 20 atm in the holding step of the processing step.
After the treatment, the treatment space was brought into conduction with the atmosphere, and the treatment space was brought to atmospheric pressure. Thereafter, only the mixed solution was taken out from the treatment apparatus.

Then, these mixed solutions were analyzed by the following method, and the presence of fulvic acid polysilica iron was confirmed.
The mixture was first filtered through a membrane filter (pore size 0.45 μm), and the filtrate was subjected to fulvic acid analysis by three-dimensional fluorescence spectrophotometry.
Next, 100 ml of the filtrate was passed through a column packed with an anion exchange resin at a rate of less than 5 ml per minute. After washing the inside of the column with distilled water, the iron complex was eluted with 40 ml of 1M hydrochloric acid, and iron and silica were quantified by ICP emission spectroscopy.
As a result, fulvic acid was measured in the former, and iron and silica bonded to fulvic acid were measured in the latter. As a result, the concentration of both was confirmed to confirm that fulvic acid polysilica iron was produced.
From the above, the effect of the present invention is clear.

  In addition, the test was conducted on the coniferous pine and cedar under the same conditions except that the treatment temperature and pressure were increased as compared with the case of the hardwood. More silica iron fulvic acid was obtained than in the case of hardwood.

Next, in the treatment space, a rice rupture material and a polysilica iron solution (Example 3), a bamboo material rupture material and a polysilica iron solution (Example 4) were used as raw materials, respectively. Manufacturing experiments were conducted.
As for the size of the ruptured material, the long side was about 10 cm on average in both cases.
The input amount was the same in both cases, and was 1.6 m ³ (80% of the volume of the processing space). In both cases, 1 kg of silica iron was added. Since rice and bamboo were dried, an appropriate amount of water was introduced together with the raw materials.

After the introduction of this raw material, the steam is stirred by the stirring means while introducing steam at a temperature of 180 ° C. for both rice and silica iron, bamboo and polysilica iron, pressure of 7 atm for rice and 12 atm for bamboo. Then, a subcritical water reaction treatment with raw material steam was performed. The treatment time is 30 minutes for rice as a raw material and 60 minutes for bamboo.
Minutes.
The state in the processing space in this processing step was set to 7 atm when the temperature was 180 ° C. and the pressure was rice, and 12 atm for the bamboo in the holding step of the processing step.

After the treatment, the treatment space was brought into conduction with the atmosphere, and the treatment space was brought to atmospheric pressure. Thereafter, only the mixed solution was taken out from the treatment apparatus.
This mixed solution was treated in the same manner as for the wood and then analyzed.

As a result, it was confirmed in the former that fulvic acid polysilica iron was produced.
From the above, the effect of the present invention is clear.

DESCRIPTION OF SYMBOLS 10 Organic waste processing device 12 Sealed container 14 Steam ejection means 16 Discharge port 18 Separation and recovery means 26 Opening and closing mechanism 30 Stirring means 50 Recovery section 52 Natural flow recovery mechanism 54 Liquid recovery flow path 58 Liquid inlet 60 Opening and closing mechanism 62 Pressure forming means 64 Same pressure communication pipe

Claims (24)

A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
A raw material charging step of charging a raw material mainly composed of wood material and polysilica iron from the supply unit into the processing space of the closed container of the processing device,
Steam having a temperature of 120 to 250 ° C. and a pressure of 5 to 35 atm is introduced into the processing space in which the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A treatment step to obtain a mixed solution containing acid polysilica iron, and
A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution by separating fulvic acid polysilica iron from the obtained mixed solution to obtain a fulvic acid polysilica iron solution. A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
A raw material charging step of charging a raw material mainly composed of wood material and polysilica iron from the supply unit into the processing space of the closed container of the processing device,
Steam having a temperature of 120 to 250 ° C. and a pressure of 5 to 35 atm is introduced into the processing space in which the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A mixed solution containing acid polysilica iron and a treatment step for obtaining a solid residue remaining in the mixed solution;
The solid residue obtained in the pretreatment step is separated from the mixed solution, the solid residue obtaining step for obtaining the solid residue, and the fulvic acid polysilica iron is separated from the mixed solution from which the solid residue is separated, A fulvic acid polysilica iron solution obtaining step for obtaining a fulvic acid polysilica iron solution is provided.   The method for producing a fulvic acid polysilica iron solution according to claim 1 or 2, wherein the wood is felled wood or waste wood.   The method for producing a fulvic acid polysilica iron solution according to claim 3, wherein the felled material is hardwood or softwood.   The method for producing a fulvic acid fulvic acid polysilica iron solution according to claim 4, wherein the broad-leaved tree is birch, willow, chestnut, oak or beech.   The method for producing a fulvic acid polysilica iron solution according to claim 4, wherein the conifer is pine, cedar, hinoki or tomato.   The method for producing a fulvic acid polysilica iron solution according to claim 3, wherein the waste material is a solid material or a plywood material.   The method for producing a fulvic acid polysilica iron solution according to any one of claims 1 to 7, wherein the treatment step is performed for 30 minutes to 12 hours.   The method for producing a fulvic acid polysilica iron solution according to claim 3, wherein the main raw material is hardwood and the pressure of the steam introduced in the treatment step is 5 to 25 atm.   The method for producing a fulvic acid polysilica iron solution according to claim 3, wherein the main raw material is conifer and the pressure of the steam introduced in the treatment step is 20 to 35 atm. A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
Into the processing space of the closed container of the processing apparatus, a raw material charging step of charging a raw material mainly composed of herbaceous material made of gramineous plants and polysilica iron from the supply unit,
While introducing the steam at a temperature of 100 to 200 ° C. and a pressure of 2 to 25 atm into the treatment space into which the raw material has been charged, the raw material is subjected to a subcritical water reaction treatment while stirring the raw material, A treatment step to obtain a mixed solution containing fulvic acid polysilica iron, and
A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution by separating fulvic acid polysilica iron from the obtained mixed solution to obtain a fulvic acid polysilica iron solution. A sealed container having a process space capable of being closed inside, a steam ejection means for ejecting high-temperature and high-pressure steam into the sealed container, a supply unit for supplying the raw material into the sealed container, and the raw material by the steam An apparatus preparation step of preparing a processing apparatus including a discharge unit for discharging the processing liquid generated by the processing to the outside;
Into the processing space of the closed container of the processing apparatus, a raw material charging step of charging a raw material mainly composed of herbaceous material made of gramineous plants and polysilica iron from the supply unit,
Steam having a temperature of 100 to 200 ° C. and a pressure of 5 to 25 atm is introduced into the treatment space where the raw material is charged, and the raw material is subjected to a subcritical water reaction treatment while stirring the raw material. A mixed solution containing acid polysilica iron and a treatment step for obtaining a solid residue remaining in the mixed solution;
The solid residue obtained in the pretreatment step is separated from the mixed solution, and the fulvic acid polysilica iron is separated from the solid residue obtaining step and the mixed solution from which the solid residue has been separated to obtain a fulvic acid silica iron solution. A method for producing a fulvic acid polysilica iron solution, comprising: obtaining a fulvic acid polysilica iron solution. The herbaceous material is a felling or cutting material, or a waste material.
Or the manufacturing method of 12 fulvic acid polysilica iron solutions.   The harvested or harvested material is any one of rice, wheat, barley, oats, rye, millet, millet, millet, sorghum, sorghum, bamboo shoot, sugar cane, pearl barley, reed, suki, sasa, danchiku, shiroganeyoshi and shiba. The method for producing a fulvic acid polysilica iron solution according to claim 13, which is based on one or more kinds.   The method for producing a fulvic acid polysilica iron solution according to claim 14, wherein the felling or cutting material is rice straw or wheat straw.   The method for producing a fulvic acid polysilica iron solution according to claim 15, wherein the felling or cutting material is bamboo.   The method for producing a fulvic acid polysilica iron solution according to claim 16, wherein the bamboo material is in a chip shape.   The method for producing a fulvic acid polysilica iron solution according to claim 11, wherein the raw material is a used waste material.   The method for producing a fulvic acid polysilica iron solution according to claim 18, wherein the waste material is an old tatami floor.   The method for producing a fulvic acid polysilica iron solution according to any one of claims 11 to 19, wherein the treatment step is performed for 30 minutes to 12 hours.   The method for producing a fulvic acid polysilica iron solution according to any one of claims 1 to 20, wherein the raw material is introduced at a volume ratio of 90% or less of the treatment space.   The method for producing a fulvic acid polysilica iron solution according to any one of claims 1 to 20, wherein the raw material is introduced at a volume ratio of 50 to 80% of the treatment space.   The method for producing a fulvic acid polysilica iron solution according to any one of claims 1 to 22, wherein the stirring in the processing step is performed by a rotating stirring member arranged in the processing space.   24. The method for producing a fulvic acid polysilica iron solution according to claim 1, wherein an alkaline solution is added as an additive in the raw material charging step.

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