WO2017175737A1

WO2017175737A1 - Cooling apparatus for carbonized biomass

Info

Publication number: WO2017175737A1
Application number: PCT/JP2017/014002
Authority: WO
Inventors: 茂也林; 龍海田野; 直秀藤本; 大輔真木
Original assignee: 宇部興産株式会社
Priority date: 2016-04-06
Filing date: 2017-04-03
Publication date: 2017-10-12
Also published as: NZ747132A; JPWO2017175737A1; MY189949A; KR20180133445A; JP7080168B2; RU2746733C2; US20190112530A1; CA3020513A1; AU2017247757A1; RU2018138556A3; RU2018138556A; AU2017247757B2

Abstract

The present invention is provided with: a carbonizing furnace for carbonizing biomass molded bodies to obtain a carbonized biomass; a classifying means which is disposed on the downstream side of the carbonizing furnace and which is for classifying the carbonized biomass; and a cooling means which is disposed on the downstream side of the classifying means and which is for cooling the classified carbonized biomass. The biomass molded bodies are molded bodies obtained by pulverization and subsequent molding of a starting material biomass, and the cooling means cools the carbonized biomass by sprinkling water thereon.

Description

Biomass carbide cooling device

The present invention relates to a biomass carbide cooling device.

Conventionally, in Patent Document 1, biocoke having excellent strength is obtained by semi-carbonizing by pulverizing biomass under pressure while heating.

Patent 4088933

However, the above-mentioned Patent Document 1 has a problem that the cooling efficiency is low because it is cooled in a pressurized state after molding and is naturally cooled by the atmosphere. Even if cooling by water cooling is performed to improve the cooling efficiency, water cooling in a pressurized state is difficult, and bio coke is biomass formed after pulverization, so that a part thereof is pulverized and handling becomes difficult. In particular, in the unsteady state where heating is not performed, the molded bio-coke may collapse and the equipment may be blocked. Or, for simplification, when carbonized (heated) and then cooled in a water tank or the like, the biomass solid fuel floats because of its low specific gravity, and the recovery becomes complicated.

The present invention has been made in order to solve the above-mentioned problems, and an object of the present invention is to reduce equipment blockage while improving the efficiency of cooling a semi-carbonized biomass molded body.

In the present invention, a carbonization furnace for carbonizing a biomass molded body to obtain a biomass carbide, provided on the downstream side of the carbonization furnace, classifying means for classifying the biomass carbide, provided on the downstream side of the classification means, and classified Cooling means for cooling the biomass carbide, and the biomass molded body is a molded body obtained by pulverizing raw material biomass and then molding, wherein the cooling means sprays the biomass carbide by watering. It is characterized by cooling.

According to the present invention, it is to reduce equipment blockage while improving the efficiency of cooling a semi-carbonized biomass molded body.

It is a figure which shows solid-state temperature -COD and pH of a biomass solid fuel. It is a figure which shows the correlation with the solid temperature in a heating process, the pulverization property of the obtained biomass solid fuel, and a grinding | pulverization speed | rate. It is a figure which shows the particle size distribution of the biomass solid fuel which performed the pulverization test. It is a figure which shows the underwater immersion test result (solid water | moisture content) of biomass solid fuel. It is a figure which shows the solid strength (rotational strength) before and behind immersion in water. It is a figure which shows the solid strength (mechanical durability) before and behind immersion in water. It is a figure which shows the BET specific surface area of a solid fuel. It is a figure which shows the average pore diameter of the surface of a solid fuel. It is a figure which shows the total pore volume of the solid fuel surface. It is a figure which shows the yield of biomass solid fuel. It is a figure which shows the spontaneous exothermic index (SCI) of biomass solid fuel. It is a cross-sectional photograph before immersion in water in Example A-2. It is a cross-sectional photograph after immersion in water (2 seconds) in Example A-2. It is a cross-sectional photograph after immersion in water (20 seconds) in Example A-2. It is a cross-sectional photograph before immersion in water in Comparative Example A. It is a cross-sectional photograph after immersion in water (2 seconds) in Comparative Example A. It is a cross-sectional photograph after immersion in water (20 seconds) in Comparative Example A. It is a figure which shows the mechanism (estimation) of solid bridge development in PBT. It is a figure which shows the result of the FT-IR analysis of the outer surface of the pellet of a biomass solid fuel. It is a figure which shows the result of the FT-IR analysis of the cross-sectional center of the pellet of biomass solid fuel. It is a figure which shows the result of the FT-IR analysis of the acetone extract of biomass solid fuel. It is a figure which shows the result of the FT-IR analysis of the solid after acetone extraction of biomass solid fuel. It is a figure which shows the result of the GC-MS analysis of the acetone extract of biomass solid fuel. It is a figure which shows the shape of the pellet after being immersed in the physiological saline in Example B. It is a figure which shows distribution of sodium before and after being immersed in the physiological saline in Example B. It is the schematic which shows the cooling equipment of biomass carbide | carbonized_material. It is the schematic which shows the other example of the cooling facility of biomass carbide | carbonized_material. It is a figure which shows the process flow of this invention. It is a figure which shows a control flow.

[Embodiment]
FIG. 26A is a schematic diagram of the present invention, and FIG. 27 is a process flow. The biomass solid fuel obtained by the fuel production process 100 of FIG. 27 becomes a product through the classification process 200 and the cooling process 300.

In the fuel production process 100, a biomass solid fuel is produced using a known method. The raw material biomass is subjected to the crushing and crushing step 110 and then molded in the molding step 120, and then heated in the heating step 130 using the kiln 1 of FIG. 26A. In the molding step 120, a binder such as a binder is not added, and the molding is simply performed by compressing and pressurizing the biomass powder.

An unheated biomass molded body (White Pellet: hereinafter referred to as WP) immediately after the molding step 120 is low in strength because it is simply pressure-molded biomass powder, and is easily pulverized during handling. Moreover, it expands and collapses due to water absorption.

In the fuel production process 100 of the present invention, the biomass molded body is heated (low-temperature carbonization) at 150 to 400 ° C. in the heating process 130 (kiln 1), so that the shape and shape of the molded body are maintained, while maintaining strength and water resistance. A biomass solid fuel (Pelletizing Before Torrefaction: hereinafter referred to as PBT) is produced. Details of the fuel manufacturing process 100 will be described later.

The classification process 200 and the cooling process 300 are performed using the vibration conveyor 2 of FIG. 26A. The vibration conveyor 2 is divided into two sections by a partition plate 24, and becomes a classification unit 21 and a cooling unit 22, respectively. The PBT discharged from the kiln 1 is transported by the vibration of the flat plate 22b and the PBT sequentially supplied from the kiln 1, and is discharged as a product through the classification unit 21 and the cooling unit 22. In addition, although the vibration conveyor 2 of FIG. 26A is inclined, the horizontal conveyor which does not incline may be sufficient.

In the classifying unit 21, the PBT and the fine powder are classified (classifying step 200) by vibrating the PBT on the sieve 21a. You may change suitably the magnitude | size of the sieve 21a according to a desired value. Those that have collapsed during manufacture or small PBT that do not reach a predetermined size fall under the sieve 21a and are processed separately. The PBT remaining on the sieve 21 a moves to the cooling unit 22.

The cooling unit 22 has a sprinkler 22a and a vibrating flat plate 22b, and the sprinkler 22a sprinkles water on the flat plate 22b. Cooling (cooling process 300) is performed by spraying water on the PBT on the flat plate 22b and discharged as a product. The cooling may be only watering, or an air nozzle or the like may be provided in addition to the watering part 22a and air cooling may be used in combination. Further, the watering nozzle may be a two-fluid nozzle of air + water.

The flat plate 22b is a smooth plate having no holes or irregularities, and a metal plate or a resin plate is used. By using a smooth plate, the PBT in the cooling unit 22 becomes slippery, and the movement in the cooling unit 22 becomes smooth.

In addition, since the classification unit 21 and the cooling unit 22 are separated by the partition plate 24, the water that has sprinkled into the cooling unit 22 is reduced from entering the classification unit 21. Thereby, the water absorption of the fine powder classified in the classification part 21 is suppressed, and the obstruction | occlusion in the classification part 21 can be reduced.

A thermometer 11 is provided at the exit of the kiln 1, and the control unit 30 executes or stops watering based on the measured temperature. The thermometer 11 may be at any other position as long as the temperature of the kiln 1 can be measured.

In the present invention, PBT having strength and water resistance is obtained only by heating WP with kiln 1, but when the temperature of kiln 1 is below a predetermined value, unheated WP or heating is not performed. Since it is insufficient, a biomass molded body in which strength and water resistance are not ensured is discharged from the kiln 1. When they are supplied to the vibrating conveyor 2, the water sprinkling unit 22 expands and collapses due to water absorption due to insufficient water resistance, causing equipment blockage.

Therefore, if the temperature measured by the thermometer 11 falls below a predetermined value, the controller 30 determines that the temperature is insufficient for PBT production and stops the watering of the watering part 22a. Thereby, even if it is a case where WP and PBT with insufficient heating are discharged when the temperature of the kiln 1 is low, collapse in the sprinkling part 22 can be suppressed and equipment blockage can be reduced.

FIG. 28 is a flowchart for continuing / stopping watering based on temperature, and is executed by the control unit 30. In step S1, the kiln 1 outlet temperature T is measured by the thermometer 11. In step S2, it is determined whether or not the measured temperature T is equal to or lower than a predetermined value α. If YES, the watering is stopped in step S3, and if NO, the watering is executed in step S4.

In particular, when the temperature of the kiln 1 is low, such as when the kiln 1 is started or unsteady, unheated WP or an under-heated biomass molded body is discharged from the kiln 1, so that collapse and equipment blockage can be achieved by stopping watering. Can be suppressed.

If the transport of WP in the kiln 1 is stopped when the kiln 1 is stopped and the temperature becomes lower than a predetermined value, the WP remains in the kiln 1. In this case, even if the temperature is low, carbonization of WP proceeds and a large amount of pyrolysis gas is generated, which is complicated because a separate gas treatment is required. Moreover, excessively carbonized WP has a small residual amount of volatile matter and is disadvantageous as a fuel, and this also needs to be treated separately, which further increases man-hours. Therefore, the conveyance stop in the kiln 1 is not preferable.

On the other hand, even if the supply of WP is interrupted at a low temperature, if the conveyance in the kiln 1 is continued, uncarbonized WP or a biomass molded body with insufficient heating will be discharged. Therefore, even when the temperature is low, the conveyance is not stopped, so that generation of a large amount of pyrolysis gas and excessive carbonization are avoided, and sprinkling to the discharged WP is stopped to prevent clogging.

The thermometer 11 directly measures the temperature of the PBT at the kiln 1 outlet, not the atmosphere temperature at the kiln 1 outlet. In the present invention, PBT (solid fuel) having water resistance and strength is obtained by carbonizing WP at a predetermined temperature or higher. However, excessive temperature rise causes carbonization to progress more than necessary, thereby deteriorating the heat yield. Therefore, fuel characteristics are inferior. Severe temperature control is required to develop water resistance and strength while ensuring the maximum heat yield, and therefore, high-precision carbonization is performed by directly measuring the temperature of the PBT. The thermometer 11 only needs to be able to directly measure the temperature of the PBT at the outlet of the kiln 1, and may be a contact thermometer or a non-contact thermometer such as an infrared ray.

[effect]
(1) A kiln 1 (carbonization furnace) that carbonizes a biomass molded body to obtain biomass carbide (PBT), and a classification unit 21 (classification means) that is provided downstream of the kiln 1 and classifies biomass carbide (PBT). A cooling unit 22 (cooling means) that is provided downstream of the classification unit 21 and cools the classified biomass carbide (PBT).
The biomass molded body was a molded body obtained by pulverizing the raw material biomass and then molded, and the cooling unit 22 cooled the biomass carbide (PBT) by watering.

When the biomass carbide is cooled by immersion in water, it is difficult to handle because the biomass carbide floats on the water and diffuses into the water surface. On the other hand, even in the case of cooling by watering, the molded biomass is easily pulverized because it forms a pulverized product. If watered as it is, biomass powder may absorb water and the equipment may be blocked. Therefore, blockage can be avoided by watering after classification. In addition to watering, air cooling and watering may be used in combination, or a two-fluid nozzle of air + water may be used.

(2) The cooling unit 22 includes a vibrating flat plate 22b (flat plate) and a sprinkling unit 22a that sprinkles water on the flat plate 22b. The flat plate 22b is a metal plate or a resin plate, and biomass carbide ( PBT) was transported.

Biomass carbide (PBT) partially collapses during transportation, so that a small amount of biomass carbide remains after classification. Smaller diameters are more likely to adhere to each other by watering, and handling during transportation tends to be complicated. Here, when cooling the biomass carbide on the net in consideration of drainage, the biomass carbide sprayed by the resistance of the irregularities of the net accumulates, and the conveyance becomes inefficient and there is a risk of blockage. Therefore, by using a metal plate or a resin plate having a low sliding resistance with the biomass carbide, it is possible to reduce the resistance during conveyance and perform efficient conveyance.

(3) When the outlet temperature of the kiln 1 is equal to or lower than a predetermined value, a control unit 30 (control means) is provided to stop watering of the watering unit 22a. In the unsteady state such as when starting and stopping, the kiln 1 is at a low temperature below a predetermined value (low temperature that is insufficient for PBT production), so that unmolded biomass (WP) or carbonization is insufficient and strength and water resistance Biomass compacts that are inferior in properties are discharged, but they swell and collapse due to watering, and there is a risk of equipment blockage. Therefore, watering can be stopped and blockage can be prevented.

(4) The thermometer 11 is capable of directly measuring the temperature of biomass carbide (PBT). PBT (solid fuel) having water resistance and strength can be obtained by carbonizing WP at a predetermined temperature or higher, while excessive carbonization deteriorates the calorie yield. Therefore, by directly measuring the temperature of the PBT, it becomes possible to perform carbonization with high accuracy, and it is possible to obtain water resistance and strength while ensuring a heat yield.

(5) A separation part 24 that separates the classification part 22 and the cooling part 23 was provided. By separating these, water intrusion into the classification unit 22 can be reduced, and accumulation and blockage during classification can be suppressed.

Instead of the vibration conveyor 2 in the above-described aspect, a classification process and a cooling process may be performed using a system as shown in FIG. 26B. This system 402 includes a vibration sieve device 403A and a cooling vibration conveyor 403B. The vibration sieve device 403A and the cooling vibration conveyor 403B are configured separately, and the vibration sieve device 403A is arranged on the upstream side in the PBT transport direction, and the cooling vibration conveyor 403B is arranged on the downstream side. Note that the description of the functions and structures common to the configuration in FIG. 26A will be omitted to avoid redundant description.

The vibration sieve device 403A has a classification unit 421 provided with a sieve 421a. On the sieve 421a, PBT is supplied from a rotary kiln (not shown in FIG. 26B) as in the configuration of FIG. 26A. The PBT is conveyed while being vibrated on the sieve 421a, whereby the PBT and fine powder are classified (classifying step). In addition, although the vibration sieve device 403A in the figure is inclined, it may be a horizontal one that does not incline.

As with the above-described embodiment, the size of the screen 421a may be appropriately changed according to a desired value. Those that have collapsed during manufacture or small PBT that do not reach a predetermined size fall under this sieve 421a and are processed separately. The PBT remaining on the sieve 421a is discharged from the discharge portion 421b of the vibration sieve device 403A.

The cooling vibration conveyor 403B has a cooling unit 422 provided with a sprinkling unit 422a, a vibrating flat plate 422b, and the like, and PBT from the vibration sieve device 403A is supplied onto the flat plate 422b. Although illustration is omitted, the cooling vibration conveyor 403B also includes a control unit that controls the operation of the watering unit 422a and the like, as in the configuration of FIG. 26A. As an example, the flat plate 422b is a smooth plate having no holes or irregularities, and a metal plate or a resin plate is used. By using a smooth plate, the PBT becomes slippery and the movement is smooth. In addition, although the cooling vibration conveyor 403B in the figure is inclined, it may be a horizontal one that is not inclined.

In this example as well, cooling may be only watering or air cooling may be used in combination. The watering nozzle may be a two-fluid nozzle of air + water. Further, similarly to the above-described embodiment, when the temperature measured by the thermometer 11 (see FIG. 26A) of the kiln 1 is lower than a predetermined value, it is controlled so that watering by the watering part 422a is stopped. Is preferable. It should be noted that the technical matters disclosed as FIG. 26B can be combined with or replaced with the contents disclosed as other aspects without departing from the spirit of the present invention.

In addition, the manufacturing method of the biomass solid fuel (PBT) manufactured in the above-mentioned fuel manufacturing process 100 is explained in full detail as follows.

[Manufacture of biomass solid fuel (PBT) in the fuel manufacturing process]
Biomass solid fuel is a molding obtained by crushing biomass after crushing, compressing and molding biomass that has become scrap or powder to form a lump, and a heating process that heats the lump after the forming process Spent solids are used as fuel (corresponding to PBT described later). Since this biomass solid fuel does not require a steam explosion process and a binder, an increase in cost can be suppressed. In the present specification, the block obtained by the molding process and before the heating step is also referred to as “unheated block”. This unheated lump corresponds to the above-mentioned WP.

The biomass used as a raw material may be woody or grassy, and the tree species and parts are not particularly limited. For example, rice pine, rice bran, cedar, firewood, European red pine, almond old tree, almond shell, acacia xylem, acacia Examples include bark, walnut shell, sago palm, EFB (empty fruit bunch of palm oil processing residue), meranti, rubber tree and the like, and may be one kind or a mixture of two or more kinds.

In the molding process, a block is formed using a known molding technique. The lump is preferably a pellet or briquette and can be of any size. In the heating step, the molded lump is heated.

The biomass solid fuel obtained after the heating step preferably has an immersion water COD (chemical oxygen demand) of 3000 ppm or less when immersed in water. The biomass solid fuel preferably has a COD ratio represented by (COD of biomass solid fuel after heating step / COD of unheated biomass solid fuel) of 0.98 or less. Here, COD (chemical oxygen demand) of immersion water when biomass solid fuel is immersed in water (also simply referred to as “COD”) refers to the preparation of an immersion water sample for COD measurement in 1973. This is the COD value analyzed according to JIS K0102 (2010) -17, in accordance with the Agency Notification No. 13 (b) Method for testing metals contained in industrial waste.

The biomass solid fuel obtained after the heating step preferably has a grindability index (HGI) based on JIS M 8801 of 15 or more and 60 or less, and more preferably 20 or more and 60 or less. Further, the BET specific surface area is preferably from 0.15 to 0.8 m ² / g, more preferably from 0.15 to 0.7 m ² / g. Further, the equilibrium moisture after immersion in water is preferably 15 to 65 wt%, and more preferably 15 to 60 wt%.

Biomass solid fuel has a fuel ratio (fixed carbon / volatile content) of 0.2 to 0.8, an anhydrous base high calorific value of 4800 to 7000 (kcal / kg), and a molar ratio O / C of oxygen O to carbon C. The molar ratio H / C of hydrogen H to carbon C is 0.8 to 1.3. When the physical property value of the biomass solid fuel is within this range, pulverization can be reduced while reducing COD in waste water during storage, and handling properties during storage can be improved. The biomass solid fuel can be obtained, for example, by adjusting the species of biomass used as a raw material, its part, the heating temperature in the heating step, and the like. The industrial analysis values, elemental analysis values, and higher calorific values in this specification are based on JIS M 8812, 8813, and 8814.

The method for producing a biomass solid fuel includes a molding step of forming biomass powder of crushed and pulverized biomass to obtain an unheated lump, and a heating step of heating the unheated lump to obtain a heated solid. The heating temperature in the heating step is preferably 150 ° C. to 400 ° C. By setting the temperature of the heating step within this range, a biomass solid fuel having the above characteristics can be obtained. The heating temperature is appropriately determined depending on the shape and size of the biomass as a raw material and the lump, but is preferably 150 to 400 ° C, more preferably 200 to 350 ° C. More preferably, it is 230 to 300 ° C. More preferably, it is 250 to 290 ° C. The heating time in the heating step is not particularly limited, but is preferably 0.2 to 3 hours. The particle size of the biomass powder is not particularly limited, but is about 100 to 3000 μm on average, preferably 400 to 1000 μm on average. In addition, the measuring method of the particle size of biomass powder may use a well-known measuring method. As will be described later, in biomass solid fuel (PBT), the connection or adhesion between biomass powders is maintained by solid crosslinking, so the particle size of biomass powders is not particularly limited as long as it can be molded. In addition, since the fine pulverization causes a cost increase, a known range may be used as long as the particle size is in a range where both cost and moldability are compatible.

It is preferable that B / A = 0.7 to 1 where A is the bulk density of the unheated mass before the heating step and B is the bulk density of the heated solid after the heating step. The value of the bulk density A is not particularly limited as long as it is a known range in which biomass powder is molded to obtain an unheated lump. Moreover, since the bulk density changes depending on the type of raw material biomass, it may be set as appropriate. Moreover, it is preferable that H2 / H1 = 1.1 to 2.5, where HGI of the unheated mass (hard glove grindability index of JIS M8801) is H1, and HGI of the heated solid is H2. By heating so that one or both of B / A and H2 / H1 are within this range, COD in wastewater during storage is reduced while reducing powdering, and handling during storage is improved. An improved biomass solid fuel can be obtained.

The characteristics of the biomass solid fuel may be determined within a suitable range depending on the species of biomass used as a raw material. One example will be described below, but the present invention is not limited to these tree species and combinations thereof. Hereinafter, preferable ranges are shown for the types of biomass raw materials used in the present invention, the properties of the obtained solid fuel (corresponding to PBT described later), and the production method thereof.

[Types of raw material biomass and properties of solid fuel]
(Yonematsu, rice straw, cedar, and firewood: solid fuel A)
As one aspect of the present invention, the properties of biomass solid fuel (hereinafter sometimes referred to as solid fuel A) when the raw material contains at least one selected from rice pine, rice bran, cedar, and straw are as follows: It is.

COD is preferably 1000 ppm or less, more preferably 900 ppm or less, further preferably 800 ppm or less, and the COD ratio is preferably 0.80 or less, more preferably 0.70 or less, and even more preferably 0.68 or less.

The equilibrium moisture after immersion in water (described later) is preferably 15 wt% to 45 wt%, more preferably 18 wt% to 35 wt%, and further preferably 18 wt% to 32 wt%.

Preferably the BET specific surface area is 0.25m ^² /g~0.8m ² / ^g, more preferably ^{0.28m 2 /g~0.6m 2 / g, 0.32m} 2 / g ~ More preferably, it is 0.5 m ² / g.

HGI is preferably 20 to 60, more preferably 20 to 55, and still more preferably 22 to 55. The HGI of coal (bituminous coal) suitable as a boiler fuel for power generation is around 50, and the closer to around 50 is preferable, considering that it is mixed and ground with coal. The HGI ratio (described later) is preferably 1.0 to 2.5.

The fuel ratio is preferably 0.2 to 0.8, more preferably 0.2 to 0.7, and still more preferably 0.2 to 0.65.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4900 to 7000 kcal / kg, and further preferably 4950 to 7000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.1 to 0.62, more preferably 0.1 to 0.61, and further preferably 0.1 to 0.60.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3, more preferably 0.85 to 1.3, and even more preferably 0.9 to 1.3.

In the above, preferred ranges for the properties of the solid fuel A are described.

In the production of the solid fuel A, the heating temperature in the heating step is preferably 200 to 350 ° C, more preferably 210 to 330 ° C, and further preferably 220 to 300 ° C.

(European red pine: Solid fuel B)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel B) when the raw material is European red pine are as follows.

COD is preferably 900 ppm or less, more preferably 800 ppm or less, further preferably 700 ppm or less, and the COD ratio is preferably 0.75 or less, more preferably 0.68 or less, and even more preferably 0.64 or less.

The equilibrium moisture after immersion in water is preferably 15 wt% to 45 wt%, more preferably 18 wt% to 40 wt%, and even more preferably 18 wt% to 31 wt%.

Preferably the BET specific surface area is 0.30m ^² /g~0.7m ² / ^g, more preferably ^{0.30m 2 /g~0.6m 2 / g, 0.30m} 2 / g ~ More preferably, it is 0.5 m ² / g.

HGI is preferably 25 to 60, more preferably 30 to 55, and even more preferably 35 to 55. The HGI ratio (described later) is preferably 1.0 to 2.5.

The anhydrous base high calorific value is preferably 4950 to 7000 kcal / kg, more preferably 5000 to 7000 kcal / kg, and further preferably 5100 to 7000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.1 to 0.60, more preferably 0.2 to 0.60, and still more preferably 0.3 to 0.60.

In the above, the preferable range in the property of the solid fuel B was described.

When producing the solid fuel B, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(Almond old wood: solid fuel C)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel C) when the raw material is an almond old tree are as follows.

COD is preferably 2100 ppm or less, more preferably 2000 ppm or less, further preferably 1500 ppm or less, and the COD ratio is preferably 0.80 or less, more preferably 0.75 or less, and further preferably 0.55 or less.

The equilibrium moisture after immersion in water is preferably 25 wt% to 60 wt%, more preferably 30 wt% to 50 wt%, and even more preferably 30 wt% to 45 wt%.

Preferably the BET specific surface area is 0.20m ^² /g~0.70m ² / ^g, more preferably ^{0.22m 2 /g~0.65m 2 / g, 0.25m} 2 / g ~ More preferably, it is 0.60 m ² / g.

HGI is preferably 15 to 60, more preferably 18 to 55, and still more preferably 20 to 55. The HGI ratio (described later) is preferably 1.0 to 2.0.

The fuel ratio is preferably 0.2 to 0.8, more preferably 0.25 to 0.7, and further preferably 0.30 to 0.65.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4800 to 6500 kcal / kg, and further preferably 4900 to 6500 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.10 to 0.70, more preferably 0.20 to 0.60, and still more preferably 0.30 to 0.60.

The molar ratio H / C of hydrogen H to carbon C is preferably 0.8 to 1.3, more preferably 0.85 to 1.3, and still more preferably 0.9 to 1.20.

In the above, the preferable range in the property of the solid fuel C was described.

In the production of the solid fuel C, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(A mixture of almond shells and old almond wood: solid fuel D)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel D) when the raw material is a mixture of almond shells and almond old wood are as follows.

COD is preferably 2500 ppm or less, more preferably 2000 ppm or less, further preferably 1500 ppm or less, and the COD ratio is preferably 0.75 or less, more preferably 0.68 or less, and further preferably 0.50 or less.

The equilibrium moisture after immersion in water is preferably 15 wt% to 50 wt%, more preferably 20 wt% to 40 wt%, and even more preferably 20 wt% to 35 wt%.

Preferably the BET specific surface area is 0.20m ^² /g~0.70m ² / ^g, more preferably ^{0.27m 2 /g~0.70m 2 / g, 0.30m} 2 / g ~ More preferably, it is 0.60 m ² / g.

HGI is preferably 20 to 60, more preferably 20 to 55, and still more preferably 23 to 55. The HGI ratio (described later) is preferably 1.0 to 2.0.

The fuel ratio is preferably 0.2 to 0.8, more preferably 0.30 to 0.7, and still more preferably 0.35 to 0.65.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4800 to 6500 kcal / kg, and further preferably 4900 to 6300 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.10 to 0.70, more preferably 0.20 to 0.60, and still more preferably 0.30 to 0.55.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3, more preferably 0.8 to 1.25, and even more preferably 0.85 to 1.20.

In the above, the preferable range in the property of the solid fuel D was described.

In the production of the solid fuel D, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(Acacia Kibe: Solid Fuel E)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel E) when the raw material is an acacia xylem are as follows.

COD is preferably 950 ppm or less, more preferably 850 ppm or less, further preferably 800 ppm or less, and the COD ratio is preferably 0.95 or less, more preferably 0.85 or less, and even more preferably 0.80 or less.

The equilibrium moisture after immersion in water is preferably 20 wt% to 60 wt%, more preferably 20 wt% to 55 wt%, and even more preferably 23 wt% to 53 wt%.

Preferably the BET specific surface area is 0.40m ^² /g~0.70m ² / ^g, more preferably ^{0.50m 2 /g~0.70m 2 / g, 0.55m} 2 / g ~ More preferably, it is 0.70 m ² / g.

The fuel ratio is preferably 0.2 to 0.6, more preferably 0.2 to 0.5, and still more preferably 0.2 to 0.4.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4800 to 6000 kcal / kg, and further preferably 4800 to 5500 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.40 to 0.70, more preferably 0.45 to 0.70, and still more preferably 0.48 to 0.65.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3, more preferably 1.0 to 1.3, and even more preferably 1.1 to 1.3.

In the above, the preferable range in the property of the solid fuel E was described.

Further, when producing the solid fuel E, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(Acacia bark: solid fuel F)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel F) when the raw material is acacia bark are as follows.

COD is preferably 2500 ppm or less, more preferably 2000 ppm or less, further preferably 1200 ppm or less, and the COD ratio is preferably 0.30 or less, more preferably 0.20 or less, and further preferably 0.15 or less.

The equilibrium moisture after immersion in water is preferably 15 wt% to 50 wt%, more preferably 20 wt% to 45 wt%, and even more preferably 25 wt% to 40 wt%.

Preferably the BET specific surface area is 0.35m ^² /g~0.55m ² / ^g, more preferably ^{0.40m 2 /g~0.55m 2 / g, 0.40m} 2 / g ~ More preferably, it is 0.50 m ² / g.

The fuel ratio is preferably 0.4 to 0.8, more preferably 0.42 to 0.75, and still more preferably 0.45 to 0.75.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 5000 to 7000 kcal / kg, and further preferably 5200 to 6500 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.25 to 0.60, more preferably 0.30 to 0.60, and still more preferably 0.30 to 0.55.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3, more preferably 0.8 to 1.2, and still more preferably 0.9 to 1.2.

In the above, the preferable range in the property of the solid fuel F was described.

In the production of the solid fuel F, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(Almond shell and walnut shell mixture: solid fuel G)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel G) when the raw material is a mixture of almond shells and walnut shells are as follows.

COD is preferably 2500 ppm or less, more preferably 2100 ppm or less, further preferably 1500 ppm or less, and the COD ratio is preferably 0.65 or less, more preferably 0.55 or less, and further preferably 0.45 or less.

The equilibrium moisture after immersion in water is preferably 20 wt% to 45 wt%, more preferably 20 wt% to 40 wt%, and even more preferably 25 wt% to 35 wt%.

Preferably the BET specific surface area is 0.15m ^² /g~0.35m ² / ^g, more preferably ^{0.19m 2 /g~0.33m 2 / g, 0.20m} 2 / g ~ More preferably, it is 0.30 m ² / g.

The HGI is preferably 18 to 60, more preferably 20 to 60. The HGI ratio is preferably 1.0 or more.

The fuel ratio is preferably 0.2 to 0.7, more preferably 0.25 to 0.65, and further preferably 0.28 to 0.60.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4800 to 6000 kcal / kg, and further preferably 5000 to 6000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.30 to 0.65, more preferably 0.40 to 0.70, and still more preferably 0.40 to 0.60.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3, more preferably 0.9 to 1.25, and even more preferably 0.9 to 1.2.

In the above, the preferable range in the property of the solid fuel G was described.

In the production of the solid fuel G, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(Sago: solid fuel H)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel H) when the raw material is sago palm are as follows.

COD is preferably 2000 ppm or less, more preferably 1600 ppm or less, further preferably 800 ppm or less, and the COD ratio is preferably 0.85 or less, more preferably 0.60 or less, and further preferably 0.4 or less.

The equilibrium moisture after immersion in water is preferably 20 wt% to 35 wt%, more preferably 20 wt% to 33 wt%, and even more preferably 22 wt% to 30 wt%.

Preferably the BET specific surface area is 0.15m ^² /g~0.35m ² / ^g, more preferably ^{0.18m 2 /g~0.33m 2 / g, 0.18m} 2 / g ~ More preferably, it is 0.30 m ² / g.

The HGI is preferably 20 to 60, more preferably 25 to 55, and even more preferably 30 to 55. The HGI ratio is preferably 1.0 to 2.5, more preferably 1.3 to 2.3, and still more preferably 1.5 to 2.2.

The fuel ratio is preferably 0.2 to 0.8, more preferably 0.25 to 0.8, and even more preferably 0.5 to 0.8.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4900 to 6500 kcal / kg, and further preferably 5000 to 6000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.20 to 0.65, more preferably 0.20 to 0.60, and still more preferably 0.2 to 0.55.

The molar ratio H / C of hydrogen H to carbon C is preferably 0.8 to 1.3, more preferably 0.85 to 1.3, and still more preferably 0.85 to 1.2.

In the above, the preferable range in the property of the solid fuel H was described.

In the production of the solid fuel H, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 290 ° C.

(EFB: Solid Fuel I)
As one aspect of the present invention, the properties of biomass solid fuel (hereinafter sometimes referred to as solid fuel I) when the raw material is EFB (empty fruit bunch of palm oil processing residue) are as follows.

COD is preferably 2350 ppm or less, more preferably 2300 ppm or less, further preferably 2000 ppm or less, and the COD ratio is preferably 0.98 or less, more preferably 0.96 or less, and further preferably 0.85 or less.

The equilibrium moisture after immersion in water is preferably 23 wt% to 45 wt%, more preferably 20 wt% to 40 wt%, and even more preferably 20 wt% to 35 wt%.

Preferably the BET specific surface area is 0.25m ^² /g~0.65m ² / ^g, more preferably ^{0.30m 2 /g~0.60m 2 / g, 0.35m} 2 / g ~ More preferably, it is 0.55 m ² / g.

The fuel ratio is preferably 0.25 to 0.8, more preferably 0.30 to 0.8, and still more preferably 0.36 to 0.8.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4900 to 7000 kcal / kg, and further preferably 5000 to 7000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.15 to 0.65, more preferably 0.15 to 0.60, and still more preferably 0.15 to 0.55.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.5 to 1.3, more preferably 0.55 to 1.3, and even more preferably 0.6 to 1.2.

In the above, the preferable range in the property of the solid fuel I was described.

In the production of the solid fuel I, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 240 to 260 ° C.

(Melanty: Solid fuel J)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel J) when the raw material is meranti are as follows.

COD is preferably 330 ppm or less, more preferably 320 ppm or less, further preferably 300 ppm or less, and the COD ratio is preferably 0.98 or less, more preferably 0.95 or less, and even more preferably 0.90 or less.

The equilibrium moisture after immersion in water is preferably 15 wt% to 30 wt%, more preferably 15 wt% to 27 wt%, and even more preferably 18 wt% to 25 wt%.

The fuel ratio is preferably 0.2 to 0.6, more preferably 0.2 to 0.5, and further preferably 0.2 to 0.45.

The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg, more preferably 4800 to 6500 kcal / kg, and further preferably 4800 to 6000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.3 to 0.60, more preferably 0.35 to 0.60, and still more preferably 0.40 to 0.60.

The molar ratio H / C between hydrogen H and carbon C is preferably 0.9 to 1.2, more preferably 0.95 to 1.2, and even more preferably 1.0 to 1.2.

In the above, the preferable range in the property of the solid fuel J was described.

In the production of the solid fuel J, the heating temperature in the heating step is preferably 200 to 350 ° C., more preferably 220 to 300 ° C., and further preferably 230 to 290 ° C.

(Rubber tree: solid fuel K)
As one aspect of the present invention, the properties of a biomass solid fuel (hereinafter sometimes referred to as solid fuel K) when the raw material is a rubber tree are as follows.

The fuel ratio is preferably 0.2 to 0.8, more preferably 0.2 to 0.7. The anhydrous base high calorific value is preferably 4800 to 7000 kcal / kg.

The molar ratio O / C of oxygen O to carbon C is preferably 0.1 to 0.7. The molar ratio H / C between hydrogen H and carbon C is preferably 0.8 to 1.3.

In the above, the preferable range in the property of the solid fuel K was described.

In the method for producing a biomass solid fuel, the present inventors, in the order of the process of performing the heating process of heating the unheated lump after the molding process, the components derived from biomass that is the raw material without using a binder. It is speculated that a biomass solid fuel with high water resistance can be produced that is used to maintain the connection or adhesion between biomass powders and does not collapse even when immersed in water. As a result of the analysis by the present inventors, the following knowledge about the mechanism by which the biomass solid fuel acquires water resistance was obtained.

The present inventors have prepared three types of biomass solid fuels having different production methods, specifically, unheated solid fuel obtained by molding pulverized biomass (White Pellet: hereinafter sometimes referred to as WP), and pulverization. The solid fuel (Pelletizing Before Torrefaction: hereinafter sometimes referred to as PBT) obtained by molding and heating the formed biomass is subjected to FT-IR analysis, GC-MS analysis, SEM observation, etc. The mechanism of water resistance of the fuel was analyzed. Note that no binder is used in either WP or PBT.

First, when the acetone extract of each solid fuel was analyzed by FT-IR, PBT obtained through the heating step had a lower content of hydrophilic COOH groups than unheated WP, but the C = C bond. It was suggested that the chemical structure of the components constituting biomass is changed by heating to become hydrophobic.

Further, when GC-MS analysis was performed on the acetone extracted components of each solid fuel, it was found that terpenes such as abietic acid and its derivatives (hereinafter also referred to as “abietic acid etc.”) thermally decomposed by heating. It is suggested that it is involved in the water resistance of fuel. Abietic acid and the like are the main components of rosin contained in pine and the like.

FIG. 18 is a diagram showing a mechanism (estimation) of solid bridge development in PBT. In the case of PBT, in the heating step after the molding step, the gap between the biomass (hereinafter sometimes referred to as biomass powder) in which the liquid due to melting of abietic acid is pulverized as the temperature rises (consolidated by molding after pulverization, Elution into the gap between adjacent biomass powders, evaporation of abietic acid and thermal decomposition occur, and the hydrophobic substance adheres to the gap between the biomass powders to develop crosslinking (solid crosslinking). Thereby, the connection or adhesion | attachment of biomass powder is maintained by the abietic acid derived from the biomass etc. which are raw materials, without adding a binder. Therefore, it is considered that the biomass powders are connected or adhered to each other to suppress water entry and improve water resistance.

On the other hand, in the case of WP, since the biomass powder is merely molded and is not heated, there is no solid bridge between the biomass powders as in the PBT. As described above, the surface of the raw biomass powder constituting the WP has a large amount of hydrophilic COOH groups and so on, making it easy for water to enter, and the invaded water greatly widens the gap between the biomass powders and is formed into pellets. Etc. easily collapse.

In addition, in the case of solid fuel molded after heating biomass powder (Pelletizing After Torrefaction: hereinafter referred to as PAT), the surface of each biomass powder itself becomes hydrophobic due to elution of abietic acid and the like. However, since it is pulverized and molded after it becomes hydrophobic by heating, it is considered that no cross-linking between biomass powders is formed like PBT. Therefore, in PAT which heats before shaping | molding, it is guessed that water penetrate | invades easily into the clearance gap between the compacted biomass powder | flour, and water resistance is inferior compared with PBT.

Abietic acid or a derivative thereof has a melting point of about 139 to 142 ° C and a boiling point of about 250 ° C. Therefore, it is inferred that heating causes abietic acid or the like to melt near the melting point to cause liquid crosslinking, and abietic acid or the like thermally decomposes near the boiling point to develop solid crosslinking.

Terpenes such as abietic acid are generally contained in biomass (Hokkaido Prefectural Forest Products Experiment Station Monthly Report No. 171, April 1966, Japan Wood Conservation Society “Wood Preservation” Vol. 34-2 (2008), etc.) . Although there is a slight difference in content depending on the type of biomass ("Use of essential oil", Oohiro Goro, Report of the 6th Research Subcommittee of the Japan Wood Society, Table 1, Table 1 of the Japan Wood Society 1999), etc. <Example A> to < In all of Examples I>, since water resistance (not disintegrated even after immersion in water, see Table 6) is exhibited by heating at 230 ° C. or higher, water resistance is generally increased by heating at least 230 ° C. to 250 ° C. for biomass in general. It is considered to be granted.

19 to 22 are diagrams showing the results of FT-IR analysis of biomass solid fuel. The raw material was European red pine of Example B below, which was obtained by analyzing a solid fuel (PBT) obtained by heating at 250 ° C., which was formed into a pellet after pulverization. The same raw material is pulverized and unheated after molding (WP) is also shown. On both the outer surface of the pellet (FIG. 19) and the center of the cross section (FIG. 20), the amount of COOH groups is WP> PBT, and the amount of C═C bonds is PBT> WP. The COOH group elution amount in the acetone extract (FIG. 21) is WP> PBT, indicating that PBT has few hydrophilic COOH groups. Furthermore, in the solid after acetone extraction (FIG. 22), PBT has more C═C bonds than WP. Therefore, it turns out that PBT is excellent in water resistance.

FIG. 23 is a diagram showing the results of GC-MS analysis of an acetone extract. The raw material is the European red pine of Example B as in FIGS. 19 to 22 above, and the solid fuel (PBT) heated at 250 ° C. after being crushed and formed into pellets and unheated (WP) are used. It was. As shown in FIG. 23, in PBT, the amount of elution of abietic acid, which is a kind of terpene, into acetone is less than that of WP, and abietic acid is melted by heating to form a liquid bridge, and then volatilization of abietic acid, etc. This is considered to indicate that a solid bridge is formed.

PBT also improves the strength of solid fuel due to the development of solid cross-linking, and has good grindability without adding a binder by heating at least 230 ° C to 250 ° C as well as water resistance (HGI, grinding speed described later). And it is inferred that good handling properties (a pulverization test described later) can be obtained. Furthermore, as described above, COD is reduced in PBT. This is because the tar content of the biomass raw material is volatilized by heating, and at the same time, the solid fuel surface of PBT is covered with solidified abietic acid, and the solid fuel surface is hydrophobic. This is considered to be because the elution of tar remaining in the biomass raw material is suppressed.

<Example A>
(Examples A-1 to A-6)
The biomass was crushed and then pulverized, and a biomass solid fuel A (PBT) was obtained through a molding process for molding the pulverized biomass and a subsequent heating process. No binder is used in any step. As a raw material biomass, a mixture of 40% by weight of rice pine, 58% by weight of rice bran, 1% by weight of cedar, and 1% by weight of rice bran was used. In the molding process of each example, it was molded into a pellet shape having a diameter of 8 mm. In the heating process in each example, 4 kg of each raw material was put into a φ600 mm electric batch furnace, heated to the target temperature in each example (heating temperature in Table 1) at a heating rate of 2 ° C./min, and heated. . Hereinafter, the target temperature and the heating temperature are the same. In each of Examples A-1 to A-6, the target temperature (heating temperature) is not maintained (the same applies to Examples B to K below). Table 1 shows the heating temperature in the heating process of Examples A-1 to A-6 and the properties of the biomass solid fuel A obtained after the heating process.

(Comparative Example A)
Comparative Example A is an unheated biomass solid fuel (WP) that has been molded after crushing and pulverization and has not undergone a heating step. In Comparative Example A, no binder is used. The raw material biomass is the same as in Example A-1. The properties of the solid fuel of Comparative Example A are also shown in Table 1.

In Table 1, as described above, HGI is based on JIS M 8801, and the higher the value, the better the grindability. Table 1 also shows the results of the higher calorific value (anhydrous basis), the fuel ratio calculated based on the industrial analysis value (air-dry basis), and the elemental analysis value (air-dry basis), and the oxygen O obtained based on this. , Carbon C, and hydrogen H, respectively.

The following analyzes were further performed on each biomass solid fuel obtained in the above examples and comparative examples.

[COD]
FIG. 1 shows the correlation between the heating temperature in the heating step and the COD (chemical oxygen demand) and pH of the immersion water when the obtained biomass solid fuel is immersed in water (the pH will be described later). The preparation of the immersion water sample for COD measurement was conducted according to JIS K0102 (2010) -17 according to the test method of metals, etc. contained in the environmental waste notification No. 13 (ii) industrial waste in 1973.

From FIG. 1, the COD of Comparative Example A (WP: biomass solid fuel that has only been molded but not subjected to the heating step) is a high value of about 1200 ppm. In contrast, biomass solid fuel heated at 230 ° C. or higher had a COD of 800 ppm or less, indicating that tar content was low. Therefore, it has been shown that the biomass solid fuels of Examples A-1 to A-6 are fuels that have less tar content and excellent handling properties even during outdoor storage. Note that the COD of the biomass solid fuels of Examples A-1 to A-6 heated at 230 ° C. or higher decreased as the heating temperature increased. This is because the COD value is reduced due to volatilization of tar content and the like accompanying heating. Since it is assumed that the temperature decreases, it is presumed that when the heating temperature is lower than 230 ° C., that is, even when the heating temperature is 150 ° C. or higher and lower than 230 ° C., the COD value is lower than that of Comparative Example A. .

[PH]
The solid fuels of Examples A-1 to A-6 and Comparative Example A were immersed at a solid-liquid ratio of 1: 3, and the pH was measured. From FIG. 1, although the values for Examples A-2 and A-3 are slightly lower, in all of Examples A-1 to A-6, the pH is approximately around 6, compared with Comparative Example A before heating. There is no particular change. Therefore, it is shown that there is no particular problem with respect to the pH of the drainage discharged when Examples A-1 to A-6 are stored outdoors.

[Crushability]
FIG. 2 shows the correlation between the heating temperature in the heating step, the pulverization property (HGI) of the obtained biomass solid fuel A, and the pulverization rate (described later), and the biomass solid fuels of Comparative Example A and Examples A-1 to A-6 It is a figure shown about.

As is clear from Table 1 and FIG. 2, in Examples A-1 to A-6, the properties changed by heating, and compared with Comparative Example A (WP: unheated biomass solid fuel), HGI (JIS M 8801) Value) is rising. The HGI of general coal (bituminous coal) is around 50, and the grinding characteristics of Examples A-1 to A-6 can be said to be better than those of Comparative Example A.

The pulverization speed in FIG. 2 was measured by measuring the weight (g / min) per unit time by measuring the weight of a 700 cc sample that was pulverized by a ball mill and passing through a 150 μm sieve as the sample after pulverization. Is. The ball mill is compliant with JIS M4002, and is used in a cylindrical container having an inner diameter of 305 mm × axial length of 305 mm. The standard grade ball bearings defined in JIS B1501 (Φ36.5 mm × 43, Φ30.2 mm × 67, Φ24.4 mm × 10 pieces, Φ19.1 mm × 71 pieces, Φ15.9 mm × 94 pieces), and rotated at a speed of 70 rpm for measurement. The pulverization rate is improved by heating, and the pulverization rate is rapidly increased particularly by heating at 230 ° C. or higher. It can be said that the pulverization rate of the biomass solid fuel A is increased and the pulverization rate is improved by elution and solidification of organic components such as tar accompanying heating. Therefore, even if the heating temperature in the heating step is 150 ° C. or higher and lower than 230 ° C., it is presumed that the HGI and the pulverization rate are improved as compared with the non-heated Comparative Example A.

[Powdering test]
Table 2 shows the cumulative ratio under sieving of the biomass solid fuel A subjected to the pulverization test, and FIG. 3 shows the particle size distribution. In order to evaluate the handling characteristics of the pellets, a pulverization test was performed. A 1 kg sample was placed in a resin bag from a height of 8.6 m and dropped 20 times, and then a rotational strength test was performed based on JIS Z 8841 to measure the particle size distribution. The obtained particle size distribution is shown in FIG. If the 2 mm sieve product in the sample particle size distribution is 30 wt% or less, and the 0.5 mm sieve product is 15 wt% or less, it is assumed that the particle size can be handled in transportation, storage, and the like. From Table 2 and FIG. 3, the sample particle size after the rotational strength test became finer as the solid temperature increased, but all the samples cleared the above-mentioned evaluation criteria, suggesting that they can be handled without problems. It was done.

[Water immersion]
Table 3 and FIG. 4 show the results of an immersion test of biomass solid fuel A in water. The solid fuel of each Example and Comparative Example was immersed in water, taken out after a predetermined time shown in Table 3 and FIG. 4, wiped off the moisture, and the solid moisture was measured. The solid fuel of Comparative Example A (WP) was disintegrated by immersion in water, and measurement of solid moisture was impossible. On the other hand, in the solid fuel of Example A-1, the water content reached equilibrium in about 10 hours after immersion, and the equilibrium water content was about 27 wt%. In the solid fuel of Example A-2, the water content reached equilibrium after about 100 hours, and the equilibrium water content was about 25 wt%. Examples A-3 to A-5 were also equilibrated at a water content of about 23 wt% after about 100 hours. Example A-6 also almost reached equilibrium after about 100 hours, and the equilibrium water content was about 28 wt% (the fluctuation is larger than in Examples A-3 to A-5, but is considered to be due to variations in raw materials). . These results are thought to be because the surface of the biomass solid fuel changed to hydrophobic due to elution and solidification of organic components such as tar with heating. Examples A-1 to A-6 (PBT) are stored outdoors. As a solid fuel, there are advantageous characteristics as a solid fuel.

[Solid strength before and after immersion in water]
(Rotational strength)
FIG. 5 shows the results of measurement of solid strength before and after immersion in water (based on JIS Z 8841 rotational strength test method) for Examples A-1 to A-6 and Comparative Example A. As described above, Comparative Example A (WP) collapsed after being immersed in water, and thus the rotational strength after immersion was not measurable. For Examples A-1 to A-6 (PBT), those obtained by wiping off the surface moisture of the solid fuel that reached the equilibrium moisture and drying it at 35 ° C. for 22 hours using a constant temperature dryer were used. The strength of Examples A-1 to A-6 (PBT) that had undergone the heating process was hardly decreased, and pulverization was less likely to occur compared to Comparative Example A (WP) before immersion in water, and handling was maintained. It can be said that it can be done.

(Mechanical durability)
FIG. 6 is a diagram showing the results of measuring the mechanical durability before and after immersion in water. For the solid fuels of Examples A-1 to A-6 and Comparative Example A, the mechanical durability DU is expressed by the following formula in accordance with American agricultural industry standard ASAE S 269.4 and German industrial standard DIN EN 15210-1. Measured based on In the formula, m0 is the sample weight before the rotation treatment, m1 is the sample weight on the sieve after the rotation treatment, and a sieve using a plate sieve with a circular hole diameter of 3.15 mm was used.

DU = (m1 / m0) × 100
Similar to the rotational strength, the mechanical durability of the examples A-1 to A-6 (PBT) that had undergone the heating process was hardly decreased, and even compared with the comparative example A (WP) before being immersed in water. It has been shown that pulverization hardly occurs and handling property can be maintained.

[Spontaneous ignition]
The evaluation was based on the “Spontaneous ignition test” of the “UN Test and Criteria Manual: Dangerous Goods Shipment and Storage Regulations 16th edition”. A measurement was made to determine whether 1 to 2 cm ³ of the biomass solid fuel (heating temperature 250 ° C.) of Example A-2 was dropped from a height of 1 m onto an inorganic heat insulating board and ignited within 5 minutes after dropping or within 5 minutes after dropping. I went twice. None of the six tests ignited, and Example A-2 (PBT) was determined not to fall under Container Class I in the United Nations Test and Criteria Manual.

[Self-heating]
As with spontaneous ignition, the evaluation was based on the “Self-Ignition Test” of the “Dangerous Goods Ship Transport and Storage Rules 16th Edition”. Fill a sample container (stainless steel cube with a side of 10 cm) with the biomass solid fuel of Example A-2 (heating temperature 250 ° C), hang it inside the thermostat, and continuously temperature the substance at 140 ° C for 24 hours. Was measured. Substances that are ignited or have a temperature rise exceeding 200 ° C are recognized as self-heating substances, and a similar test is conducted using a sample container with a side of 2.5 cm. It was confirmed. Based on the test results, Example A-2 (PBT) was determined not to be a self-heating substance.

[Pore size distribution]
(BET specific surface area)
FIG. 7 is a graph showing the measurement result of the BET specific surface area of the solid fuel A. For the solid fuels of Examples A-1 to A-6 and Comparative Example A, using an automatic specific surface area / pore diameter distribution measuring device (BELSORP-min II manufactured by Nippon Bell Co., Ltd.), the sample was adjusted to 2 to 6 mm as a pretreatment. After being cut and filled into a container, vacuum deaeration was performed at 100 ° C. for 2 hours to obtain a BET specific surface area. Nitrogen gas was used as the adsorption gas. FIG. 7 shows that the BET specific surface area increases with increasing heating temperature, and that pores develop with heating (pyrolysis).

(Average pore diameter, total pore volume)
FIG. 8 shows the average pore diameter on the surface of the solid fuel A, and FIG. 9 shows the total pore volume. Both the average pore diameter and the total pore volume were measured using the same apparatus as the BET specific surface area. The “pore” here is a pore having a diameter of 2 nm to 100 nm. Since the average pore diameter decreases with increasing heating temperature in Example A-2 and later, it shows that many fine pores are generated. This is believed to be due to cellulose degradation.

[yield]
FIG. 10 shows the yield (solid yield and heat yield) of biomass solid fuel A after the heating step. The solid yield is the weight ratio before and after heating, and the heat yield is the calorific value ratio before and after heating. Note that, as described above, holding at the target temperature (heating temperature) of each example is not performed (the same applies to Examples B to K below).

From the results of Examples A-1 to A-6 above, according to the present invention, biomass solid fuel A (PBT) with reduced COD, improved grindability, reduced water absorption, improved solid strength, and improved yield is obtained at low cost. It was shown that

[Spontaneously exothermic]
The natural heat generation property of the solid fuel of Example A-2 was measured by the following method. 1 kg of the sample was placed in a container, the reactor was placed in a constant temperature bath at 80 ° C., and the O 2, CO, and CO 2 concentrations of the gas obtained by flowing air through the sample were measured. The O2 adsorption amount, CO generation amount, and CO2 generation amount based on the heating of the sample are calculated from the concentration before and after heating, and the spontaneous exothermic index (SCI) is calculated based on the following equation (1).

Natural exothermic index (SCI)
= {O2 adsorption amount * O2 adsorption heat * (1/100)} + {CO generation amount * (CO production heat + (1/2) * H2O production heat * H / C) * (1/100)}
+ {CO2 generation amount * (CO2 generation heat + (1/2) * H2O generation heat * H / C) * (1/100)} (1)

The adsorption amount, generation amount, and H / C in the solid fuel of Example A-2 are as follows.

O2 adsorption amount 0.42 [ml / kg ・ min]
CO emissions 0.03 [ml / kg ・ min]
CO2 generation 0.02 [ml / kg ・ min]
H / C (Molar ratio of hydrogen and carbon in the solid fuel of Example A-2) 1.28 [mol / mol] (see Table 1)
Further, the heat of adsorption and the heat of formation used in the formula (1) are as follows.

O2 adsorption heat 253 [kJ / mol] (same value as O2 adsorption heat on coal)
CO generation heat 110.5 [kJ / mol]
Heat of H2O generation 285.83 [kJ / mol]
CO2 generation heat 393.5 [kJ / mol]
Based on the above, the SCI of the solid fuel according to Example A-2 was calculated to be SCI = 1.3. In addition, since the property of biomass solid fuel A is close to that of coal, the same heat of adsorption of O2 as that of adsorption on coal was used.

Using the same method as the calculation of SCI in Example A-2, SCI was also calculated for Examples A-1 to A-3, A-6 and Example A-2 after the pulverization test (see Table 2 and FIG. 3). did. The calculation results are shown in FIG. For comparison, FIG. 11 also shows SCI of bituminous coal in Table 4. The horizontal axis in FIG. 11 is arrival-based moisture, and the SCI of bituminous coal in FIG. 11 is prepared by adding moisture to the bituminous coal shown in Table 4 and preparing four types of samples each having different moisture. The SCI is calculated.

As the SCI value is lower as shown in the formula (1), it can be said that the spontaneous exothermicity is lower. Therefore, Examples A-1 to A-3, A-6, and Example A-2 after the pulverization test (Table 2 and FIG. 3) and bituminous coal, if the water content is similar, the biomass solid fuel (PBT) of the present invention has a lower SCI (spontaneously exothermic) than bituminous coal and is comparable to high moisture bituminous coal. SCI (spontaneously exothermic). Thereby, it can be said that the biomass solid fuel A (PBT) is a good fuel with reduced risk of ignition during handling.

[Surface photo]
12 to 14 are cross-sectional SEM photographs of the solid fuel (PBT) before and after immersion in water in Example A-2. 12 is before immersion, FIG. 13 is after 2 seconds immersion, and FIG. 14 is after 20 seconds immersion. Similarly, FIGS. 15 to 17 are cross-sectional SEM photographs before and after immersion in water in Comparative Example A (WP), FIG. 15 is before immersion, FIG. 16 is after immersion for 2 seconds, and FIG. 17 is after immersion for 20 seconds. In both Example A-2 and Comparative Example A, the cross section after immersion is a cross section obtained by cutting the solid fuel after immersion for 2 seconds or 20 seconds. The magnification and scale are shown below each photo.

Comparing the photographs before and after immersion in water, in Comparative Example A (FIGS. 15 to 17), the pores are enlarged after immersion in water. Since this is a molded product of biomass in which Comparative Example A (WP) is pulverized as described above, it is presumed that the biomass was absorbed by water soaking and pores (gap between biomass powders) were enlarged. Accordingly, it is considered that the pulverized biomass is separated from each other by further intrusion of moisture into the enlarged pores, and the solid fuel itself collapses (see FIG. 4).

In contrast, the pores of the solid fuel surface of Example A-2 (FIGS. 12 to 14) are not enlarged even after being immersed in water, and the change due to immersion is small. In Example A-2, solid bridges develop between the biomass powders by heating, the hydrophobicity is improved and it is difficult to absorb water, and it is presumed that there is little change due to immersion. Therefore, even after immersion, since the connection or adhesion between the pulverized biomass by solid crosslinking is maintained, it is unlikely to collapse as in Comparative Example A. Therefore, in the heated solid fuels of Examples A-1 to A-6 (PBT), as shown in FIG. 4, biomass solids in which collapse due to rain water or the like is suppressed and handling properties during outdoor storage are ensured. Fuel has been obtained.

<Example B>
In Example B-1 to Example B-4 (PBT), the temperature was raised to the target temperature (heating temperature described in Table 5) in the same manner as in Example A except that European red pine was used as the raw material biomass. did. Tables 5 and 6 show properties of the solid biomass fuel B (Example B-1 to Example B-4) obtained after the heating step. Comparative example B (WP) was shown in the same manner. As in Example A, no binder is used in any of Examples B-1 to B-4 and Comparative Example B. Since the moisture after immersion in water is after immersion for 100 hours or more (168 hours in Example B), it is considered that the moisture in the solid fuel B has substantially reached equilibrium. The measuring method of each property of the biomass solid fuel is the same as in Example A above. The ball mill grindability described in Table 6 was measured as follows.

[Ball mill grindability]
The pulverization time of each biomass solid fuel B was 20 minutes, and the weight ratio under a 150 μm sieve after 20 minutes was used as a pulverization point. In addition, the ball mill uses what conforms to JIS M4002, and uses a standard class ball bearing (Φ36.5 mm × 43, Φ30.2 mm × 67, Φ36.5 mm × 67 Φ24.4 mm × 10 pieces, Φ19.1 mm × 71 pieces, Φ15.9 mm × 94 pieces), and rotated at a speed of 70 rpm for measurement. The higher the value, the better the grindability. It was confirmed that the pulverization point increased as the heating temperature increased.

Comparative Example B disintegrated immediately after being immersed in water. In contrast, in Examples B-1, B-3 and B-4, the biomass powders were kept connected or adhered to each other even after being immersed in water (168 hours) and did not collapse. As a result, the solid shape was maintained after immersion, so that moisture measurement was possible and the expression of water resistance could be confirmed. In addition, pulverization is improved and COD is reduced as compared with Comparative Example B. Example B-3 is particularly excellent from the viewpoint of water resistance (moisture after immersion), and the biomass solid fuels of Examples B-2 and B-3 exhibit particularly excellent physical properties from the viewpoint of yield.

Also, it is estimated that Example B-2 is a fuel having excellent water resistance and pulverization properties and reduced COD based on the development of solid bridges.

<Example C>
The raw material biomass was heated to the target temperature (heating temperature described in Table 5) and heated (Example C-1 to Example C-4: PBT) in the same manner as in Example A, except that almond old wood was used. . The ball mill grindability was measured by the same method as in Example B above. Tables 5 and 6 show properties of the biomass solid fuel C obtained after the heating step. As in Example B, the water after immersion in water is considered to be balanced because it is after immersion for 100 hours or longer (168 hours in Example C). Comparative example C (WP) was shown in the same manner. In Examples C-1 to C-4 and Comparative Example C, no binder is used.

Comparative Example C disintegrated immediately after being immersed in water. On the other hand, in all of Examples C-1 to C-4, the connection or adhesion between the biomass powders is maintained even after being immersed in water, and the water resistance is improved without being destroyed. In addition, improvement in grindability and reduction in COD are shown. From the viewpoint of COD and water resistance (moisture after immersion), Example C-2, Example C-3 and Example C-4 are excellent, and from the viewpoint of thermal yield, Example C-1, Example C-2 and Example C- 3 is excellent. The HGI of Example C-1 is lower than that of Comparative Example C, but this is considered to be due to variations in raw materials and measurement errors, and it is estimated that there is at least an HGI equivalent to or higher than that of Comparative Example C. .

<Example D>
The raw material biomass was heated to the target temperature (heating temperature described in Table 5) and heated (Example D-1) in the same manner as in Example A, except that (30 wt% almond shell + 70 wt% almond old wood) was used. -Example D-4: PBT). The ball mill grindability was measured by the same method as in Example B above. Tables 5 and 6 show properties of the biomass solid fuel D obtained after the heating step. The water after immersion in water is assumed to be balanced after immersion for 100 hours or more (168 hours in Example D). The same applies to Comparative Example D (WP). In Examples D-1 to D-4 and Comparative Example D, no binder is used.

Comparative Example D disintegrated immediately after being immersed in water. On the other hand, in all of Examples D-1 to D-4, even after immersion in water, the connection or adhesion between the biomass powders is maintained, so that they do not collapse and the water resistance is improved. In addition, improvement in grindability and reduction in COD are shown. Examples D-2, D-3, and D-4 are excellent from the viewpoint of COD, and Examples D-1, D-2, and D-3 are particularly excellent from the viewpoint of thermal yield. showed that.

<Example E>
The temperature was increased to the target temperature (heating temperature described in Table 5) in the same manner as in Example A, except that Acacia xylem was used as the raw material biomass, the biomass was molded into a tablet shape, and a φ70 mm tubular furnace was used as the heating device. Warmed and heated (Example E-1 to Example E-3: PBT). Properties of the biomass solid fuel E obtained after the heating step are shown in Tables 5 and 6. The water after immersion in water is considered to be balanced after immersion for 100 hours or more (168 hours in Example E). The same applies to Comparative Example E (WP). In Examples E-1 to E-3 and Comparative Example E, no binder is used. In Example E, the pH was measured by immersing the solid fuel at a solid-liquid ratio of 1:13. Here, the immersion time of Comparative Example E in Table 6 indicates that the pH was measured, that is, the pH after 96 hours had elapsed after Comparative Example E was immersed.

Comparative Example E disintegrated immediately after immersion in water, but Examples E-1 to E-3 maintained water resistance without disintegration because the connection or adhesion between the biomass powders was maintained. Examples E-2 and E-3 are excellent from the viewpoint of water resistance (water after immersion in water), and Examples E-1 and E-2 are excellent from the viewpoint of heat yield. In Example E, PBT heated at 240 to 270 ° C. is presumed to have formed the above-mentioned solid crosslinks, and is considered to have excellent water resistance, COD, pulverization properties, and the like. Further, the heat yield of Example E-1 exceeds 100%, but this is due to variations in raw materials and measurement errors.

<Example F>
The temperature was raised to the target temperature (heating temperature described in Table 5) and heated (Example F-1 to Example F-4: PBT) in the same manner as in Example E except that acacia bark was used as the raw material biomass. Tables 5 and 6 show the properties of the solid biomass fuel F obtained after the heating step. The water after immersion in water is considered to be balanced after immersion for 100 hours or more (168 hours or more in Example F). The same applies to Comparative Example F (WP). In Examples F-1 to F-4 and Comparative Example F, no binder is used. In Example F, the pH was measured by immersing the solid fuel at a solid-liquid ratio of 1:13. Here, the immersion time of Comparative Example F in Table 6 indicates that the pH was measured, that is, the pH after 96 hours had elapsed after Comparative Example F was immersed.

Comparative Example F disintegrated in 1 hour after being immersed in water, but Examples F-1 to F-4 maintained the water resistance without disintegration because the connection or adhesion between the biomass powders was maintained. Examples F-2, F-3, and F-4 are excellent from the viewpoint of COD and water resistance (moisture after immersion in water), and Examples F-1, F-2, and F are preferable from the viewpoint of thermal yield. -3 is excellent.

<Example G>
The temperature was raised to the target temperature (heating temperature described in Table 5) in the same manner as in Example A except that (70 wt% almond shell + 30 wt% walnut shell) was used as the raw material biomass and a φ70 mm tubular furnace was used as the heating device. And heated (Example G-1 to Example G-4: PBT). Properties of the biomass solid fuel G obtained after the heating step are shown in Tables 5 and 6. Water after immersion in water is considered to be in equilibrium after being immersed for 100 hours or longer (144 hours or longer in Example G). The same applies to Comparative Example G (WP). In Examples G-1 to G-4 and Comparative Example G, no binder is used.

Comparative Example G disintegrated immediately after being immersed in water, but Examples G-1 to G-4 maintained the connection or adhesion between the biomass powders and exhibited water resistance without disintegration. Examples G-2, G-3, and G-4 are excellent from the viewpoint of COD and water resistance (moisture after immersion in water), and Examples G-1 and G-2 and G are preferable from the viewpoint of thermal yield. -3 is excellent. The thermal yield of Example G-2 exceeds 100%, but this is due to variations in raw materials and measurement errors.

<Example H>
The sample was heated to the target temperature (heating temperature described in Table 5) and heated (Example H-1 to Example H-4: PBT) in the same manner as in Example A, except that sago palm was used as the raw material biomass. The ball mill grindability was measured by the same method as in Example B above. Properties of the biomass solid fuel H obtained after the heating step are shown in Tables 5 and 6. The water after immersion in water is considered to be balanced after immersion for 100 hours or more (168 hours in Example H). The same applies to Comparative Example H (WP). In Examples H-1 to H-4 and Comparative Example H, no binder is used. The immersion time of Comparative Example H in Table 6 indicates that the pH was measured, that is, the pH after 24 hours had elapsed after Comparative Example H was immersed.

Comparative Example H disintegrated in 3 hours after immersion in water, but Examples H-1 to H-4 maintained water resistance without disintegration because the connection or adhesion between biomass powders was maintained. Example H-2, Example H-3, and Example H-4 are excellent from the viewpoint of COD, pH (slightly low) and water resistance (moisture after immersion in water), and Example H-1 and Example from the viewpoint of thermal yield H-2, example H-3, is excellent.

<Example I>
The sample was heated to the target temperature (heating temperature described in Table 5) and heated (Example I-1) in the same manner as in Example A, except that EFB (empty fruit bunch of palm oil processing residue) was used as the raw material biomass. ~ Example I-4: PBT). Properties of the biomass solid fuel I obtained after the heating step are shown in Tables 5 and 6. The water after immersion in water is assumed to be balanced after immersion for 100 hours or more (168 hours in Example I). The same applies to Comparative Example I (WP). In Examples I-1 to I-4 and Comparative Example I, no binder is used.

The mechanical durability before and after immersion in water for Example I-3 heated at 270 ° C. and Example I-4 heated at 300 ° C. was measured by the following method. A sample of 50 g is filled in a 1,000 cc polypropylene container, and is rotated with a MISUGI mixing man SKH-15DT at 60 rpm for 30 minutes (total 1,800 revolutions). The sample after rotation is sieved with a sieve having a circular hole diameter of 3.15 mm, and the following formula:
DU = (m1 / m0) × 100
Was used to calculate mechanical durability (DU). In the formula, m0 is the sample weight before the rotation treatment, and m1 is the sample weight on the sieve after the rotation treatment.

Comparative Example I disintegrated immediately after immersion in water, but Examples I-1 to I-4 maintained the connection or adhesion between biomass powders and exhibited water resistance without disintegration. Examples I-2, I-3, and I-4 are excellent from the viewpoint of COD and water resistance (moisture after immersion in water), and Examples I-1, I-2, and I are excellent from the viewpoint of thermal yield. -3 is excellent.

<Example J>
The sample was heated to the target temperature (heating temperature described in Table 5) and heated (Example J-1, Example J-2: PBT) in the same manner as in Example A except that Meranti was used as the raw material biomass. Properties of the biomass solid fuel J obtained after the heating step are shown in Tables 5 and 6. The water after immersion in water is considered to be balanced after immersion for 100 hours or more (168 hours in Example J). The same applies to Comparative Example J (WP). In all of Examples J-1, J-2, and Comparative Example J, no binder is used.

Comparative Example J disintegrated immediately after being immersed in water, but Examples J-1 and J-2 maintained water resistance without disintegration because the connection or adhesion between the biomass powders was maintained. Excellent results were also shown for COD.

<Example K>
The sample was heated to the target temperature (heating temperature described in Table 5) and heated (Example K) in the same manner as in Example A, except that a rubber tree was used as the raw material biomass and a φ70 mm tubular furnace was used as the heating device. -1). Table 5 shows properties of the biomass solid fuel K obtained after the heating step. The same applies to Comparative Example K (WP). In any case, no binder is used.

As for the comparative example K, it is expected to collapse by immersion in water as in the other examples. On the other hand, with respect to Example K-1, the formation of the above-mentioned solid bridge is expected to improve water resistance, pulverization, reduce COD, etc. without being disintegrated even when immersed in water. Example K-1 is heated at 270 ° C., but the same effect can be estimated for a heating temperature of 230 to 270 ° C. as described above.

<Water absorption distribution>
In order to compare the water resistance of PAT and PBT, the distribution of sodium after water absorption was examined for these biomass solid fuels using saline. As a sample of PAT, a solid fuel obtained by heating a raw European red pine at 250 ° C. and then molding the pellet into a pellet having a diameter of 6 mm was used. As a PBT sample, a solid fuel (solid fuel B) heated at 250 ° C. after forming a raw red pine as a 6 mm diameter pellet was used. PBT and PAT were immersed in 0.9 wt% physiological saline for 5 days. As a result, as shown in FIG. 24, the PBT retained the pellet shape (left in FIG. 24), but the PAT collapsed greatly (right in FIG. 24). Further, before immersion of PAT and PBT in physiological saline and after immersion in 0.9 wt% physiological saline for 5 days, the sections were subjected to EPMA (Electron Probe MicroAnalyzer) analysis, and the Na distribution was compared. As for Na distribution, PBT remained on the pellet surface and did not penetrate inside, whereas PAT was widely distributed even inside (see FIG. 25). This means that PBT has less saline intrusion than PAT. Also from this result, PBT prevents the invasion of water because the pyrolysis product of the extraction component is solid-crosslinked in the gap between adjacent biomass powders and becomes hydrophobic. Since water can penetrate into the gap, water penetrates to the inside of the pellet, and as a result of pushing the gap between the biomass powders, it is assumed that it has collapsed.

[Expansion coefficient before and after immersion in water]
The pellet length before and after immersion in water was measured for the solid fuels of Examples A-1 and A-3. For the pellet length, 10 pellets before immersion were selected and measured with an electronic caliper (Mitutoyo: CD-15CX, the repeatability was 0.01 mm, and the two decimal places were rounded off) and the same. After immersing the pellet in water for 72 hours, the length was measured again with an electronic caliper. In addition, when the pellet end was slanted before and after immersion, the length up to the tip was measured. Table 7 shows the measurement results. As shown in Table 7, the pellet length of Example A-1 increased by an average of 4.6%, and Example A-3 increased by an average of 0.2%.

* In Table 7, the same sample does not correspond to the same row.

Further, with respect to the solid fuels of Examples A-1 to A-6, the pellet diameters before and after immersion were measured by the same electronic caliper and measurement method as those in Table 7. Table 8 shows the measurement results. The measured value of the pellet diameter is an average value of 10 randomly selected in each of Examples A-1 to A-6.

Tables 7 and 8 show that the expansion rate decreases as the temperature of the heating process increases. It is presumed that the expansion is suppressed by the formation of solid crosslinks accompanying heating. Although the radial expansion coefficient in Table 8 is higher than the length expansion coefficient in Table 7, this is because the immersion time is longer in Table 7, and because Example A is a pellet, it is mainly consolidated in the radial direction. Therefore, it is considered that the expansion also increases in the radial direction. In Table 8, the expansion coefficient is 10% or less even in Example A-1 having the largest radial expansion coefficient. In Example A, the diameter and length expansion coefficient is preferably 10% or less, and more preferably 7% or less. The volume expansion coefficient is preferably 133% or less, and more preferably 123% or less.

In Tables 7 and 8, the expansion rates of Example A are shown. Based on Table 6, the expansion rates of Examples B to J are calculated. In the same manner as in Example A, the expansion coefficient was calculated using the following formula (2).

Expansion rate = {(value after immersion−value before immersion) / value before immersion} × 100 (2)

Example B is a pellet, and the diameter expansion coefficient calculated using the pellet diameter before immersion (initial dimension in Table 6) and the pellet diameter after immersion (dimension after immersion in Table 6) based on the formula (2) is It was 15% or less (hereinafter, the expansion coefficient of the diameter after Example B uses the formula (2)). As in Example A, it is estimated that the length expansion coefficient is smaller than the radial expansion coefficient in the pellet. Therefore, when the volume expansion coefficient is calculated on the assumption that the length expansion coefficient in Example B is 15% or less at the maximum, 152% or less (before immersion) The volume after immersion with respect to the volume of 100% is also the same for Example C and the following. In Example B, the radial expansion coefficient is preferably 20% or less, and more preferably 10% or less. The volume expansion coefficient is preferably 173% or less, and more preferably 133% or less.

Example C is also a pellet, and the volume expansion coefficient is 123% or less on the assumption that the diameter expansion coefficient before and after immersion is 7.2% or less and the length expansion coefficient is 7.2% at the maximum. Similarly, the volume expansion coefficient is calculated). The diameter expansion coefficient in Example C is preferably 13% or less, and more preferably 7% or less. The volume expansion coefficient is preferably 144% or less, and more preferably 123% or less.

For Example D (pellet), the expansion coefficient before and after immersion is 8.8% or less, and the volume expansion coefficient based on it is 129% or less. The diameter expansion coefficient in Example D is preferably 10% or less, and more preferably 8% or less. The volume expansion coefficient is preferably 133% or less, and more preferably 126% or less.

Example E has a tablet shape, the diameter (φ) expansion coefficient is 2.5% or less, the height (H) expansion coefficient is 40% or less, and the volume expansion coefficient is 147% or less. The radial expansion coefficient is preferably 5% or less, and more preferably 2.3% or less. The height expansion coefficient is preferably 50% or less, and more preferably 20% or less. The volume expansion rate is preferably 165% or less, and more preferably 126% or less.

Example F (tablet) has a diameter expansion coefficient of 4.0% or less, a height expansion coefficient of 15% or less, and a volume expansion coefficient of 124% or less. Note that the height after immersion in Example F-3 is considered to be a measurement error or individual variation. The expansion coefficient is preferably 5% or less, and more preferably 3% or less. The height expansion coefficient is preferably 40% or less, and more preferably 10% or less. The volume expansion coefficient is preferably 154% or less, and more preferably 117% or less.

For example G (pellet), the expansion coefficient before and after immersion is 8.8% or less, and the volume expansion coefficient based on it is 129% or less. The expansion coefficient is preferably 10% or less, and more preferably 8% or less. The volume expansion coefficient is preferably 133% or less, and more preferably 126% or less.

For Example H (pellet), the expansion coefficient before and after immersion is 6.9% or less, and the volume expansion coefficient based on it is 122% or less. The radial expansion coefficient is preferably 10% or less, and more preferably 7% or less. The volume expansion coefficient is preferably 133% or less, and more preferably 123% or less.

For Example I (pellets), the expansion coefficient before and after immersion is 4.1% or less, and the volume expansion coefficient based on it is 113% or less. The expansion coefficient is preferably 10% or less, and more preferably 5% or less. The volume expansion rate is preferably 133% or less, and more preferably 116% or less.

For Example J (pellet), the diameter expansion coefficient before and after immersion is 5.4% or less, and the volume expansion coefficient based on it is 117% or less. The expansion coefficient is preferably 20% or less, and more preferably 10% or less. The volume expansion coefficient is preferably 173% or less, and more preferably 133% or less.

As described above, the solid fuel (PBT) of the present invention using biomass as a raw material preferably has an expansion coefficient of 40% or less before and after immersion (including diameter and height). Is preferably about 275% or less. More preferably, the expansion coefficient of diameter and length is 30% or less, and the volume expansion coefficient is about 220% or less. More preferably, the expansion coefficient of diameter and length is 20% or less, and the volume expansion coefficient is about 173% or less. More preferably, the expansion coefficient of diameter and length is 10% or less, and the volume expansion coefficient is about 133% or less. Thus, when the expansion rate after immersion in water is within a certain range, it is indicated that the biomass solid fuel (PBT) does not collapse even by immersion and has water resistance.

In addition, PBT was separately prepared and tested for each material of rubber tree, acacia and meranti. The test results are shown in Tables 9 and 10 below. In the test results of Table 9 and Table 10, rubber tree is described as example a, acacia is described as example b, and meranti is described as example c.

DESCRIPTION OF SYMBOLS 1 Carbonization furnace 2 Vibrating conveyor 11 Thermometer 21 Classification part (classification means)
22 Cooling unit (cooling means)
22a Watering part (watering means)
22b Flat plate 24 Separation part 30 Control part (control means)
100 Fuel production process 110 Grinding process 120 Molding process 130 Heating process 200 Classification process 300 Cooling process 402 System 403A Vibration sieve device 403B Cooling vibration conveyor 421 Classification part 421a Sieve 421b Discharge part 422 Cooling part 422a Sprinkling part 422b Flat plate

Claims

A carbonization furnace for carbonizing a biomass molded body to obtain biomass carbide,
A classification means provided on the downstream side of the carbonization furnace for classifying the biomass carbide;
A cooling means provided on the downstream side of the classification means, and for cooling the classified biomass carbide,
The biomass molded body is a molded body obtained by pulverizing raw material biomass and then molding,
The said cooling means cools the said biomass carbide | carbonized_material by watering. The cooling device of the biomass carbide | carbonized_material characterized by the above-mentioned.
The biomass carbide cooling device according to claim 1,
The cooling means has a vibrating plate and a watering part that sprays water on the plate,
The said flat plate is a metal plate or a resin plate, and conveys the said biomass carbide | carbonized_material by vibration, The biomass carbide | carbonized_material cooling device characterized by the above-mentioned.
In the biomass carbide cooling device according to claim 1 or 2,
A thermometer for measuring the temperature of the carbonization furnace outlet is provided,
A biomass carbide cooling apparatus, comprising: a control unit that stops the watering unit when the temperature measured by the thermometer becomes a predetermined value or less.
The biomass carbide cooling device according to claim 3,
The said thermometer can directly measure the temperature of the said biomass carbide | carbonized_material. The cooling device of the biomass carbide | carbonized_material characterized by the above-mentioned.
In the biomass carbide manufacturing apparatus according to any one of claims 1 to 4,
A biomass carbide cooling apparatus, comprising: a separating section that separates the classification means and the cooling means.