TWI320840B - Entrained bed gasification system for solid biomass carbonization and the method thereof - Google Patents

Description

IX. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a gasification reactor for a belt bed, and in particular to a continuous carbonization of a powdery biomass energy raw material, which is produced - Biomass carbon can be gasified to produce synthetic gas using high temperature and oxygen-deficient conditions. • Solid biomass energy carbonization combined with belt gasification system and its process. [Prior Art] # Gasification reaction is an incomplete combustion reaction of hydrocarbons under high temperature and oxygen deficiency. 'Coal gasification has been applied for more than 100 years. In the early stage, it provided the city's gas (Town Gas) as the second world. During the war, Germany used it to produce transportation fuel. Advanced gasification technology is an important clean coal technology. It began to develop in the United States in the beginning of the year. It mainly hopes to replace coal and natural gas that is subject to short-term factors and rising prices. Another expectation is that #展展The factory, therefore, the birth of the first commercial coal gasification power plant located in California, USA, φ 5 10 paintings. In addition to power generation, coal gasification can be used to produce a wide range of products such as industrial gases, chemical raw materials, hydrogen and methanol fuels. f comes to the principle of clean coal technology, with single-finger environmental control, but emphasizes high energy efficiency and targets ultra-low pollution. Because gasification technology can not only be diversified (for example: electricity, fuel, chemicals), but also can use various feed (such as: coal, petroleum coke, biomass and waste) characteristics, so the application potential is the most I am optimistic. In terms of energy efficiency improvement, integrated energy and electricity waste with new generation efficiency, that is, combined with coal gasification and with 6 1320840 liquid methanol fuel process, high efficiency gas and thirsty wheel-based re-cycle power generation and local temperature Integrated power plants for fuel cells are the target. Coal „divided into fixed bed, fluidized bed and sling bed. The three main 挟 π beds are high efficiency and high energy density gasification reactor, while fixed bed and fluidized bed are more suitable for medium and small gas (4). Coal-carbon gasification can produce a low-carbon composite body _, so compared to the direct combustion energy recovery method, the summer is inclined to provide a more environmentally friendly technology than the gas, but gasification

It will produce tar with high viscosity and easy to cause pipeline blockage, which will make the utilization and storage of synthetic gas very difficult. Complex decoking equipment becomes a necessity for gasification biomass energy system. The high-temperature gasification reaction of the gas-bed reactor with 挟 can avoid the generation of tar' is the gasification reactor mainly used in large-scale coal gasification and recirculation power plants. The amount of biomass energy produced by photosynthesis in plants is equivalent to about 100-100 million tons of coal heat equivalent per year. Such a large amount of biomass energy exceeds the world's annual energy consumption by seven times. Currently, biomass energy is the most used renewable energy in the world.

One of the sources. Although the 挟-bed gasification reactor also has the ability to feed multiple materials, if the feed heat value is low or the reactivity is low, the conditions of high-temperature gasification will not be formed. 6 The main components of the biomass are cellulose and wood. The main constituent elements are carbon (45%~50%), oxygen (40%~45%), hydrogen (5〇/.~1〇./0), and the calorific value is about half of the coal (3000Kcal/ Kg), the low energy density makes the biomass less used in advanced gasification reactors. However, biomass energy is a self-produced renewable energy source. A large amount of biomass energy can greatly increase Taiwan's energy security. And effectively reduce the carbon dioxide emissions in the island. 1320840 The existing sputum bed gasification reactor mainly uses the dry and wet method to inject carbon powder and pure oxygen into the furnace, and vaporizes the pulverized coal by the heat released by partial combustion or anaerobic combustion. Synthetic gas is produced (for example: C〇, ch4). Such an anthracite bed gasification reaction furnace generates money for a further use. However, in order to increase the gasification efficiency of the synthesis gas, the following invention is produced. SUMMARY OF THE INVENTION Accordingly, the present invention is directed to providing a solid biomass energy carbonization combined with an annulus bed gasification system and a process thereof (4) a biomass energy carbonization process for biomass energy having a low calorific value or a low energy density. First converted into high-energy Pangu reaction intensity of biomass energy carbon, the biomass energy carbon is ground to about 50 micro' meters: simultaneously injected with pure oxygen into the belt bed gasifier for high-efficiency gasification reaction plant. The other purpose is to provide a solid biomass energy carbonization combined with an annulus bed gasification system and a process thereof, which is to increase the gasification conversion of the gasification furnace of the anthracene bed by using the raw carbon energy in the gas bed of the crucible bed. Efficiency and reduction of air pollution emissions, because the biomass energy carbon contains low impurities, and almost no sulfur, and the reaction intensity of biomass carbon is higher than fossil coal, which is the most Good feed source. The present invention is also directed to providing a solid biomass energy carbonization combined with an annulus bed gasification system and a process thereof, which utilizes combustion of biomass energy carbonization gas in a gasification furnace to generate high temperature gas in the gasification furnace. The conditions can be used to create a more rapid gas reduction, and also reduce the formation of tar (4) due to the reduced temperature and long residence time, so the gasification reaction rate and strength of the gasification reaction of the 8 1320840 furnace can be improved. The tar contained in the synthetic gas (syngas) can be greatly reduced. According to the above object of the present invention, a solid biomass energy carbonization combined with an annulus bed gasification system is provided, comprising a biomass gasification furnace providing a carbonization heat source, a biomass indirect heating carbonization furnace, a grinding unit, and a挟With bed gasifier. The biomass can indirectly heat the carbonization furnace, and has a carbonization furnace body, and at least one of the carbonization furnace bodies is separated into one another.

a partition between a second space and a feed port for continuously feeding a plurality of carbon material into the first space, a heat source input end for introducing the carbonization heat source, and each independently and in communication with the first space a gas output end and a solid output end 'and a heat source output end communicating with the second space and away from the heat source output end. The grinding unit provides grinding of the carbon material, and

The feed port is connected to the solid output end, and the feed port of the pulverized powdery biomass carbon material is sent out. The belt bed gasification furnace has a gas bed with a gas bed, a gas inlet connected to the gas output end, and a solid adjacent to the gas inlet and connected to the feed port of the grinding unit a inlet, a first oxygen supply end adjacent to the gas introduction port, a second oxygen supply end adjacent to the solid introduction port, the gas introduction port, the solid introduction port, the first oxygen supply end, and the a gas combustion zone defined by the second oxygen supply end, and a gas outlet port remote from the gas introduction port and the solid introduction port. Thereby, the first and second oxygen supply ends respectively send oxygen into the rolling body combustion zone, so that the high-temperature gaseous and powdery biomass energy introduced into the milk combustion zone through the gas introduction port and the solid introduction port respectively The carbon material is burned to produce gasified synthetic gas. 9 1320840 In accordance with the above objects of the present invention, a solid biomass energy carbonization bonded crucible bed gasification process is provided which comprises the following manufacturing steps: (A) providing a carbonization heat source and a carbon material feedstock, respectively. (B) introducing the carbonization heat source and the carbon material into a biomass to indirectly heat the carbonization furnace to respectively generate a high temperature carbonized gas and a biomass carbon material. (C) grinding the biomass carbon material into micronized particles. (D) introducing the high-temperature carbonized gas and the micronized powdered biomass carbon material into a gas-bed bed gasifier respectively, and respectively adding oxygen at the inlet of the guide to enable high-temperature carbonized gas and powdery biomass The carbon material is rapidly gasified into a gasified synthetic gas (syngas). According to an embodiment of the present invention, the biomass energy having a low calorific value or a low energy density is first converted into a biomass energy having a high calorific value and a high reaction intensity by using a biomass carbonization program, and the biomass carbon is ground to about 50. After the micrometer, it is injected into the gasifier with a pure bed of oxygen at the same time to carry out a high-efficiency gasification reaction. According to an embodiment of the present invention, the gasification conversion efficiency of the gasification furnace of the anthracene bed bed is improved and the air pollution emission is reduced by using the biomass energy carbon in the gas bed furnace, because the biomass carbon has low impurities. It is almost free of sulfur, and the reaction strength of biomass carbon is higher than that of fossil coal. It is the best source of feed for gas beds. According to an embodiment of the present invention, by burning a biomass gas in a gasification furnace, high-temperature gasification conditions can be generated in the gasification furnace, and a faster gasification reaction can be achieved, and the gasification can be reduced because of low gasification. The temperature and the long residence time of the tar (tar) form a problem, so the gasification reaction rate and strength of the gas bed reactor can be increased, so that the tar contained in the synthetic gas (syngas) can be greatly reduced. 10 132ΌΜΌ f 狮7朗城作力正正

According to the above, the solid biomass energy carbonization combined with the belt bed gasification system of the present invention and the process thereof can vaporize the biomass energy having half of the coal value into high quality synthetic gas, and the synthetic gas can replace the increasingly short The use of natural gas or liquefied petroleum gas as a high-efficiency recirculation t (four) is self-produced and belongs to the biomass energy of the Portuguese-salmon, which can effectively reduce carbon dioxide emissions and increase energy autonomy. [Embodiment] FIG. 1 is a system combination diagram showing an embodiment of a solid biomass energy carbonization bonded crucible bed gasification system according to an embodiment of the present invention. Referring to Fig. 1, a solid biomass energy carbonization combined with an annulus bed gasification system according to an embodiment of the present invention comprises a biomass gasifier (9), a biomass indirect heating carbonization furnace 200, and a grinding unit 300. , a storage tank 400, a pump 500 ' and a 挟 belt bed gasifier 6 〇〇. Referring to Fig. 2, a detailed structural diagram of the biomass gasifier 1〇〇 and the high pressure blower 140 of the present invention is shown. Referring to Fig. 3, the supply of the biomass gasifier and the raw material supply tank is shown. A partial enlargement of the feedstock entering the biomass to heat the carbonization furnace. Refer to Figure 1, Figure 2 and Figure 3. The biomass gasifier 1 has a gasification furnace body 110, an embedded combustion tube 120, a gasification air tube 130, and a high pressure blower 14A. The biomass fuel enters the cylindrical gasifier from the upper biomass feed port 111. A row of gray grid barriers 116 at the bottom supports the entire reactor. During the combustion process, the biomass fuel passes through a drying zone 112, a thermal cracking zone 113 and a reduction zone 114 by gravity, and the last char is fully in the combustion zone 115 of the furnace bottom and the air. Mix until the char is completely burned to ash and then dropped into a ash tank 117 of the bottom layer. The biomass gasifier 100 is evacuated by a high-pressure blower 14 to provide a combustion zone 115 for combustion of carbon through a gasification air tube 130 on the upper surface of the hearth along the columnar surface to forcefully feed the gasification air toward the center. The air needed. The combustion air required for the combustion tube 122 in the biomass gasification furnace 100 is also introduced into the combustion air by the high-pressure blower 140, mixed with the gasification gas from the furnace, and completely burned and discharged. The synthetic gas produced in the reduction zone 114 and the pyrolysis zone 13 enters the built-in combustion tube through the plurality of pores 121 of the lower half of the inner combustion tube 12. The built-in combustion tube 12 is not only a passage for supplying synthetic gas to the gasification furnace via the exhaust pipe 123, but also a combustion chamber for synthesizing gasification gas. The synthetic gasification gas is mixed with the externally introduced secondary combustion air in the internal combustion pipe 120 and completely burned into a high temperature and clean exhaust gas, and the main component of the exhaust gas is carbon dioxide (c〇2) and water. (HA) and nitrogen (nj, excess oxygen can be controlled to a very low degree, and the exhaust gas contains no tar and fly ash. The biomass gasifier of the present invention is 1 〇〇, and the biomass fuel is moved downward. While the gasification synthesis gas is in a countercurrent upward combustion mode, the biomass combustion is dried in the drying zone 112, and is thermally cracked in the thermal cracking zone 113 of the anoxic high temperature to generate pyrolysis gas and char, drying and The thermal energy required for thermal cracking is mainly provided by the exhaust gas from the combustion of the charcoal in the hearth combustion zone 115, and the radiant heat of the combustion zone U5 also contributes partially. In the reduction zone 114, the C02 and H2 are borrowed from the multi-boolean (B〇und〇urarcj) The reaction reacts with water vaporization 12 1320840 (water-shift) to reduce c产生 and Η2, and the final residual carbon is thoroughly mixed with air in the combustion zone 115 of the bottom of the furnace until the charcoal After completely burning into ash, it falls into the ash storage tank 117 of the bottom layer.

In addition, the present invention places a built-in combustion tube 120 in the thermal cracking zone 113, and the built-in combustion tube 120 provides a process in which the synthetic gas is directly burned off without decoking inside the gasification furnace. Rich C〇 and Η. Therefore, the combustion intensity is high, and the high-temperature exhaust gas and the combustion tube can maintain the high temperature environment required for the thermal cracking zone 113. The thermal cracking strength and temperature of the biomass fuel can be much higher than that of the conventional fixed gasifier. Referring to Fig. 4, a partial enlarged view of the indirect heating of the carbonization furnace 2, the grinding unit 300, and the storage tank 400 is shown. Refer to Figures 1 and 4. The biomass can indirectly heat the carbonization furnace 2, and has a carbonization furnace body 210, and a compartment 220 that divides the carbonization furnace body 21 into one of the first space 211 and the second space 212. A plurality of carbon material raw materials 23 〇 are continuously fed into the feed port 240 of the first space 2 ι, a heat source input end 250 for introducing the carbonization heat source 〇1,

a gas output end 26 and a solid output end 270, each of which is independent of the first space 211, and a heat source output end 280 that communicates with the second space 212 and away from the heat source input end 250. In this embodiment, the biomass indirect heating carbonization furnace 2 is an annular barrel, and the partition 220 is a ring body for separating the first and second spaces 2U, 212. The grinding unit 300 is used for grinding the raw lunar carbon 230 produced by the solid wheel outlet 27 into micron-sized particles (about 5 micrometers). The grinding unit 13 1320840

There is a feed port 310 for introducing the raw biomass carbon material 230' produced by the solid output end 270, and a feed port 320 for feeding the pulverized powdery biomass carbon material 230". Referring to Figure 5, A partial enlarged view showing the simultaneous addition of powdered and gasified biomass to the gasification furnace of the belt bed. Referring to Figures 1 and 5, the pump 500 is connected to the feed port of the grinding unit 300. 320 is interposed between the solid introduction port 630 of the crucible bed gasification furnace 600 for pumping micron-sized powdery biomass carbon material 230" into the crucible bed gasification furnace 600. Refer to Figures 1 and 4. The storage tank 400 is connected between the polishing unit 300 and the pump 500 for storing the ground powdery biomass carbon material 230". Referring to Figures 1 and 5, the belt bed gas The furnace 600 has a gas bed furnace body 610, a gas inlet port 620 connected to the gas output end 280, and a gas inlet port 620 adjacent to the gas inlet port 620 and connected to the feed port 320 of the grinding unit 300. a solid inlet 630, a first oxygen supply end 640 adjacent to the gas introduction port 620, a second oxygen supply end 650 adjacent to the solid introduction port 630, a gas inlet port 620 and the solid introduction port. a gas outlet 670 of the 630, and a gas combustion zone 660 between the gas introduction port 620, the solid introduction port 630, the first oxygen supply end 640 and the second oxygen supply end 650. When the first The two oxygen supply ends 640 and 650 respectively send oxygen (02) into the gas combustion zone 660, and the high temperature gaseous and powdery biomass energy carbon material 230" is instantaneously partially burned (the temperature of the gas combustion zone 600 is as high as 1400 °C). C or so), to quickly produce high-quality 14 1320840 cargo year / Qiao: 丨 quality Gasification Synthesis gas (syngas). In addition, the gasification syngas produced by the crucible bed gasifier 600 is directed to a purification unit (not shown) at the rear end for processing. Referring to the block diagram of Fig. 6, a flow chart of the gasification process of the solid biomass energy carbonization combined with the belt bed according to an embodiment of the present invention is shown. Referring to Figures 1 and 6, the solid biomass carbonization combined with an annulus bed gasification process of the present invention comprises the following steps: Step 1: As in Process 801, the carbonization is produced via the Biomass Gasifier 100. Heat source 101. In the process 802, the carbon material raw material 230 is supplied through a raw material supply tank 700, and the preparation operation of the carbonization heat source 101 and the carbon material raw material 230 is first performed. Step 2: According to the process 803, the carbonization heat source 101 is sent to the second space 212 of the biomass energy indirect heating of the carbonization furnace 200. The carbon material raw material 230 is introduced into the first space 211 of the carbonization furnace 200 by indirect heating, and the high temperature carbonization gas and the biomass energy carbon material are respectively generated by the high temperature indirect heating treatment by the partition portion 220. 230'. Step 3: As in Process 804, the grinding energy unit 230' is used to grind the biomass energy carbon material 230' into a powdery biomass carbon material 230" having a particle size of about 50 microns, and is stored in the storage tank 400. Step 4: In step 804, the micronized powdered biomass carbon material 230" is pumped into the ankle belt bed gasifier 600 via the solids introduction port 630 by the pump 500. As in flow 805, the high temperature carbonized gas produced at the gas output 620 is introduced into the annuncleated bed gasifier 600 through the gas introduction port 620. As in the process 806, the flow 807 and the flow 808, when the powdery biomass 15 1320840 carbon material 230" is simultaneously introduced into the 挟 belt bed gasifier 600 and the high temperature carbonized gas, the guide is also at the inlet: The first and second oxygen supply ends 640 and 650 are respectively added with oxygen (02), so that the high temperature carbonized gas and the powdery biomass energy carbon material 230" are rapidly and instantaneously partially burned into gasified synthetic gas (syngas) in the gas combustion zone 660. As in flow 809, the synthetic gas (syngas) is finally output from the gas outlet 670. The temperature of the gas combustion zone 660 is as high as about 1400 ° C, and the main component of the high temperature carbonized gas is a combination of H20 and co2. The two components react with the injected bioenergy carbon material in a Boulderour reaction and a water-shift reaction, respectively, and the reaction formula is as shown in formula (1) and formula (2): C02 gasification reaction (Boudouard) Reaction): C (biocarbon) + C〇2 &lt;-&gt; 2CO (1) H20 gas 4 gas reaction reaction: C (biocarbon) + H2O · 〇 · CO + H2 (2) According to The combustion biomass in the gas-bedded gasifier 600 can indirectly heat the carbonized gas generated in the carbonization furnace 200, and can generate high-temperature gasification conditions in the gas-bedded gasifier 600, which can not only produce a faster gasification reaction. The problem of formation of tar due to low gasification temperature and long residence time can also be reduced, so that the present invention can improve the gasification reaction rate and strength of the gasification reactor of the bismuth bed, and the synthesis gas (syngas) The tar (tar) will be greatly reduced. In summary, the solid biomass energy carbonization combined with the belt bed gasification system of the present invention and the process thereof have the following effects and advantages: 16 1320840 1. Compared with the existing anthracite bed gasification reactor is by dry and wet The way to inject carbon powder and pure oxygen into the furnace 'only use the heat released by partial combustion or anaerobic combustion to gasify the pulverized coal to produce synthetic gas (c〇, H2, CH4, etc.) The disadvantage of poor quality. The present invention injects the high calorific value carbonized gas (i.e., high temperature carbonized gas) and the milk gas (〇2) generated by the biomass indirectly by the carbonization furnace 200 into the gas combustion zone 600, and the gas combustion zone 600 is at about 1400 t: High-temperature rapid and instantaneous partial combustion, in order to quickly produce gasification and syngas with high efficiency and high purity (purity), it can improve the gasification reaction rate and strength of the gasification reactor of the belt bed, so as to greatly reduce the synthesis. The amount of tar contained in the gas (syngas). In the present invention, the carbonization type in which the carbonization furnace 200 is indirectly heated by the carbonization heat source 101 by the biomass energy can increase the carbonization rate and the calorific value of the carbonized gas. In addition, in the present embodiment, the biomass = indirect heating carbonization furnace 200 is agitated by a spiral shaft (not shown), and the biomass carbon material 230 is moved to the solid output end 27〇 for continuous feeding. The double-layered door that is linked with the continuous discharge is used, so the invention has a fast production speed and can increase the output. Third, the use of biomass energy carbonization program 'will be low calorific value or low energy density of biomass can be converted into high calorific value and high reaction intensity of biomass energy carbon, biomass energy carbon after grinding to about 50 microns, can be temporarily It is stored in the storage tank 400, or directly injected into the gasification furnace of the belt bed with pure oxygen (〇2) to carry out high-efficiency gasification reaction in order to achieve the expected gas efficiency and quality.四4. Injecting the raw material energy carbon material into the 挟 belt bed gasifier 3〇〇, not only can improve the gas conversion efficiency of the 挟 belt bed gasifier _ 降低 降低 降低 降低 ψ ψ The raw material carbon material contains low impurities and contains almost no sulfur, and the reaction strength of the raw material carbon material is higher than that of the fossil coal. Therefore, the present invention utilizes the powdered biomass which is carbonized and micronized at room temperature. The carbon material is 23 〇, and it is introduced into the 挟 belt bed gasifier 600 for gasification reaction, which is an optimal feed source. Therefore, the solid biomass energy carbonization combined with the belt bed gasification system of the present invention and the process thereof can vaporize the biomass energy having half of the carbon value into high-quality synthetic gas, and the synthetic gas can be replaced by the increasingly short Natural gas or liquefied petroleum gas, as a fuel for high-efficiency double-cycle power generation, borrows a large amount of self-produced 'and is the biomass energy in carbon dioxide, which can effectively reduce carbon dioxide emissions and increase energy autonomy. Although the present invention has been disclosed in an embodiment of the present invention, it is not intended to limit the present invention, and it is obvious to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention. The scope of protection is subject to the definition of the scope of the patent application attached. BRIEF DESCRIPTION OF THE DRAWINGS The above and other objects, features, advantages and embodiments of the present invention will become more <RTIgt; A flow chart of a combination of equipment for biomass carbonization combined with an annulus bed gasification system. Fig. 2 is a view showing the detailed structure of the biomass gasifier of this embodiment. Fig. 3 is a partially enlarged view showing the biomass gasification furnace and the raw material supply tank of the embodiment. Fig. 4 is a partially enlarged view showing the (4) indirect heating of the carbonization furnace and the grinding unit and the storage tank of the biomass in this embodiment. Fig. 5 is a partially enlarged view showing the belt bed gasifier and the pump of the embodiment. Fig. 6 is a flow chart showing the steps of a gasification process for a solid biomass energy carbonization knotted mantle belt bed according to an embodiment of the present invention. . 〇【Main component symbol description】 100 : Biomass gasifier 101 : Carbonization heat 110 : Gasifier body 111 : Biomass energy feed port 112 : Drying zone 113 : Thermal cracking zone 114 : Reduction zone 115 : Combustion zone 116 : Ash gate 117 : Ash storage bucket 120 : Built-in combustion pipe 121 : Pork 122 : Burning pipe 123 : Exhaust pipe 140 : High pressure blower 130 : Gasified air pipe 200 : Biomass energy indirectly heats the carbonizing furnace 210 :Carbide body 211 : First space 212 : Second space 220 : Zone 2 3 0 : Carbon material raw material 230 ': Biomass carbon material 230'': Powdery biomass carbon material 240 : Feed port 250: heat source input 260: gas output 270: solid output 1320840

280: heat source output terminal 300: grinding unit 310: inlet port 320: discharge port 400: storage tank 500: Lipu 600: 挟 belt bed gasifier 610: 挟 belt bed gasification furnace body 620: gas inlet port 630 : Solids inlet 640 : First oxygen supply end 650 : Second oxygen supply end 660 : Gas combustion zone 670 : Gas outlet 700 : Raw material supply tank 801 : Process 802 : Process 803 : Process 804 : Process 805 : : Process 806: Process 807:: Process 808: Process 809: : Process 20

Claims (1)

1320840 X. Patent application scope: A kind of solid biomass energy carbonization combined with an annulus bed gasification system, comprising: raw material, the gasification furnace provides a carbonization heat source; the raw material side indirectly heats the carbonization furnace, has a carbonization furnace body, at least a partitioning portion for dividing the carbonization furnace body into a first space and a second space, a feed port for continuously feeding a plurality of carbon material raw materials into the first space, and a feeding source for introducing the carbonization heat source a heat source input end, a gas output end and a solid output end respectively connected to the first space of the first space, and a heat source output end communicating with the second space and away from the input end of the heat source; a feed port for introducing the raw material carbon material produced at the solid output end and a feed port for discharging the pulverized powdery biomass carbon material; and a belt bed gasifier having a sling band a gasification furnace body, a gas inlet port connected to the gas output end, a solid inlet port adjacent to the gas inlet port and connected to the feed port of the grinding unit, adjacent to the oxygen a first oxygen supply end of the inlet, a second oxygen supply end adjacent to the solid introduction port, a gas outlet port remote from the gas introduction port and the solid introduction port, and a gas inlet port, the solid a gas combustion zone between the inlet, the first oxygen supply end and the second oxygen supply end; thereby, when the first and second oxygen supply ends respectively send oxygen into the gas combustion zone, respectively The gas introduction port and the high-temperature gaseous and powdery biomass carbon material introduced into the gas combustion zone by the solid introduction port are partially burned, and the produced gas 21 is synthesized into a gas. 2. The solid biomass energy carbonization combined with the belt bed gasification system as described in claim 1 of the patent application includes a pump. 3. The solid biomass energy carbonization combined with a belt bed gasification system as described in claim 2, wherein the pump is connected between the feed port of the grinding unit and the solid introduction port of the belt bed gasifier . 4. The solid biomass energy carbonization combined with a belt bed gasification system as described in claim 1, wherein the grinding unit grinds the biomass energy carbon material into micron-sized particles. 5. The solid biomass energy carbonization combined with an annulus bed gasification system as described in claim 4, wherein the grinding unit grinds the raw f energy carbon material into 5 〇 micrometers and then feeds into the 挟 belt bed gasifier. . 6. The solid biomass energy carbonization combined with the belt bed gasification system as described in claim 5, further comprising a storage tank, wherein the ground powdery biomass energy carbon material is stored in the storage tank. 7. The solid biomass energy carbonization combined with the bed gasification system as described in claim 1 of the patent scope, wherein the temperature of the gas (four) burning zone is about 1400 °C. 22 8. The solid biomass energy carbonization combined with the belt bed gasification system as described in claim 1 wherein the biomass indirect heating carbonization furnace is an annular barrel, and the partition is used to separate a ring body of the first and second spaces. 9. The solid biomass energy carbonization combined with an annulus bed gasification system as described in claim 1, wherein the biomass gasification furnace has a gasification furnace body, a built-in combustion tube, and a gasification An air tube having a raw material feed inlet and a combustion zone. 10. The solid biomass carbonization combined crucible bed gasification system of claim 9, wherein the gasification furnace body further has a drying zone, and the drying zone is located above the combustion zone. 11. The solid biomass energy carbonization, '·° σ挟 bed gasification system according to claim 10, wherein the gasification furnace body further has a thermal cracking zone, wherein the thermal cracking zone is located in the drying zone Between the burning zones. 12. The solid biomass energy carbonization combined with an annulus bed gasification system according to claim 11, wherein the gasification furnace body further has a reduction zone, the reduction zone being located between the thermal cracking zone and the combustion zone . 13. The solid biomass energy carbonization combined with an annulus bed gasification system according to claim 12, wherein the gasification furnace body further has an ash storage tank, and the storage ash tank is located below the reduction zone. 14. The solid biomass energy carbonization combined crucible bed gasification system according to claim 9, wherein the combustion tube is connected to a combustion tube and an exhaust tube respectively. 15' The solid biomass energy carbonization combined with the belt bed gasification system according to claim 9 of the patent application scope, wherein the biomass gasification furnace further comprises a high pressure blower, the pressure blower and the built-in combustion tube and The gasification air tube is connected. 16· The solid biomass energy carbonization combined with the belt gasification system according to claim 9 of the patent scope, the gasification furnace body further has a thermal cracking zone, and the built-in combustion pipe has a plurality of through pipes The pores of the wall, and the pores are in communication with the pyrolysis zone. 1?·—A kind of solid biomass energy carbonization combined with a belt gasification process' includes the following manufacturing steps (A) providing a carbonization heat source and a carbon material raw material respectively; (B) the carbonization heat source and the carbon material At the same time, a primary inductive energy is introduced to indirectly heat the liquefaction furnace to respectively generate a high-temperature carbonized gas, and a primary biomass &amp; stone counter material; '(C) grinding the biomass carbon material into micronized particles; and (D) The high-temperature carbonized gas and the micronized powdered biomass energy carbon material 1320840 are introduced into the 抉-bed gasification furnace, and oxygen is added to the guiding population, respectively, so that the high-temperature carbonized gas is difficult to be purely produced. Gasification into gasification synthesis gas. 18. For the solid biomass energy carbonization combined with the belt gasification process as described in Item 17 of the scope of the patent application, before the step (9), the powdered biomass energy carbon material is pumped into the belt bed gas using the Lipu pump. In the furnace. 19. The solid biomass energy carbonization combined with the belt bed gasification process as described in claim 17 of the patent application. The carbonization heat source is produced by a biomass gasifier. 25