JP6048133B2 - Syngas generation system and synthesis gas generation method - Google Patents

Description

  The present invention relates to a synthesis gas generation system that generates synthesis gas and a synthesis gas generation method.

  In recent years, a technology has been developed that gasifies raw materials such as coal, biomass, and tire chips to generate synthesis gas instead of petroleum. Synthetic gas generated in this way is used for power generation systems, hydrogen production, synthetic fuel (synthetic petroleum) production, chemical fertilizer (urea) and other chemical products. Among the gasification raw materials used as the raw material for synthesis gas, coal, in particular, has a recoverable period of about 150 years, more than three times the recoverable period of oil, and reserves are unevenly distributed compared to oil. Therefore, it is expected as a natural resource that can be stably supplied over a long period of time.

  Conventionally, the gasification process of coal has been performed by partial oxidation using oxygen or air. However, since it is necessary to perform partial oxidation at a high temperature of 2000 ° C., there is a disadvantage that the cost of the gasification furnace increases. Had.

  In order to solve this problem, a technology for gasifying coal at about 700 ° C. to 900 ° C. using water vapor has been developed. In this technology, it is possible to reduce the cost by setting the temperature low, but the generated synthesis gas contains tar as compared with the synthesis gas generated by partial oxidation at a high temperature of 2000 ° C. Many were included. When the temperature of the synthesis gas is lowered in such a process using the synthesis gas, tar contained in the synthesis gas is condensed, resulting in problems such as blockage of piping, failure of equipment used in the process, poisoning of the catalyst, and the like. End up.

  Thus, a technique for removing particles such as tar contained in the synthesis gas by spraying water on the synthesis gas generated in the gasification furnace is disclosed (for example, Patent Document 1).

  However, since tar is hydrophobic, its affinity with water is low. Therefore, even if water is sprayed on the synthesis gas as in the technique of Patent Document 1, tar cannot be sufficiently removed from the synthesis gas.

  Therefore, a technique for removing tar contained in synthesis gas by spraying synthesis gas with oil having high affinity with tar instead of water is disclosed (for example, Patent Document 2).

JP 2005-41959 A Japanese Patent No. 3934402

  In Patent Document 2 described above, since the oil after washing the synthesis gas (oil after washing) contains tar, the oil after washing is first separated from tar and then cooled by a cooler. Then, it is used again for cleaning the synthesis gas. Therefore, the heat energy of the oil after washing has been discarded by the cooler. Moreover, the cost for discarding the separated tar was required.

  In view of such a problem, the present invention can efficiently remove tar from synthesis gas by washing the synthesis gas with oil having high affinity with tar, and can use the oil after washing. It is an object to provide a synthesis gas generation system and a synthesis gas generation method that can effectively use the thermal energy of oil after washing by devising it, and can effectively use the removed tar. It is said.

In order to solve the above-described problems, a synthesis gas generation system of the present invention includes a combustion furnace for heating a fluidized medium, a fluidized medium heated by the combustion furnace, and water vapor , thereby forming a fluidized bed of the fluidized medium. A gasification furnace that gasifies the gasification raw material with the heat and water vapor of the fluidized bed to generate synthesis gas, and the generated synthesis gas and oil are brought into contact with each other, thereby bringing the synthesis gas into contact with the oil. An oil cleaning section to be cleaned, a post-cleaning oil that is an oil after the syngas is cleaned in the oil cleaning section, and a sedimentation separation section that separates water from the washed oil by a difference in specific gravity, and a sedimentation separation section comprising an oil portion for sending post-wash oil water is separated into the combustion furnace, and a water portion for sending water separated by settling section to the gasifier, the combustion furnace, the fluidized medium Characterized by using the cleaning after oil to heat.

  The oil delivery unit may send the washed oil to a gasification furnace, and the gasification furnace may gasify the washed oil as a gasification raw material.

In order to solve the above problems, the synthesis gas generation process of the present invention includes a combustion furnace for heating the fluidized medium, and the fluidized medium heated by the combustion furnace, is introduced and the water vapor, a fluidized bed of the fluidized medium A synthesis gas generation method using a gasification furnace that is formed and gasifies a gasification raw material with heat and water vapor of the fluidized bed to generate synthesis gas, the generated synthesis gas and oil A step of cleaning the synthesis gas with the oil by contacting, a step of storing the washed oil that is the oil after washing the synthesis gas, and separating water from the washed oil according to the difference in specific gravity; It includes a step of sending the oil after washing from which water has been separated to one or both of the combustion furnace and the gasification furnace, and a step of sending the separated water to the gasification furnace .

  In the present invention, by washing the synthesis gas with oil having high affinity with tar, tar can be efficiently removed from the synthesis gas, and by devising the use destination of the oil after washing, It becomes possible to effectively use the thermal energy of the oil, and further to effectively use the removed tar.

It is explanatory drawing for demonstrating the synthesis gas production | generation system concerning 1st Embodiment. It is a flowchart for demonstrating the flow of a process of the synthesis gas production | generation method concerning 1st Embodiment. It is explanatory drawing for demonstrating the synthesis gas production | generation system concerning 2nd Embodiment. It is a flowchart for demonstrating the flow of a process of the synthesis gas production | generation method concerning 2nd Embodiment. It is explanatory drawing for demonstrating the synthesis gas production | generation system of a modification.

  Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. The dimensions, materials, and other specific numerical values shown in the embodiments are merely examples for facilitating the understanding of the invention, and do not limit the present invention unless otherwise specified. In the present specification and drawings, elements having substantially the same function and configuration are denoted by the same reference numerals, and redundant description is omitted, and elements not directly related to the present invention are not illustrated. To do.

(First embodiment: synthesis gas generation system 100)
FIG. 1 is a diagram for explaining a synthesis gas generation system 100 according to the first embodiment. As shown in FIG. 1, the synthesis gas generation system 100 includes a synthesis gas generation device 110 and a synthesis gas purification device 200. In Fig. 1, the flow of gas (gas) is indicated by solid arrows, the flow of sand is indicated by dashed-dotted arrows, the flow of gasification raw materials is indicated by double-dotted arrows, and the flow of liquids such as water and oil is outlined. Indicated by an arrow.

  The synthesis gas generation system 100 is a technology for generating synthesis gas by gasifying solid raw materials such as coal, biomass, tire chips, etc., instead of petroleum. Examples of coal include peat, lignite, lignite, subbituminous coal, bituminous coal, semi-anthracite, and anthracite.

  In the synthesis gas generation system 100, a gasification raw material is gasified at about 700 ° C. to 900 ° C. using steam in a gasification furnace in which a fluid medium forms a fluidized bed (steam gasification). In this synthesis gas generation system 100, it is possible to reduce the cost for raising the temperature by setting the temperature low, but the synthesis gas produced is a synthesis produced by partial oxidation at a high temperature of 2000 ° C. Compared to gas, a large amount of tar is contained. Therefore, the synthesis gas purification apparatus 200 is used to purify the produced synthesis gas. Hereinafter, specific configurations of the synthesis gas generation apparatus 110 and the synthesis gas purification apparatus 200 will be described in that order.

(Syngas generator 110)
As shown in FIG. 1, the synthesis gas generation device 110 includes a combustion furnace 112, a medium separation device (cyclone) 114, a gasification furnace 116, and a boiler 118.

In the synthesis gas generator 110, as a whole, a fluid medium composed of sand such as dredged sand (silica sand) having a particle size of about 300 μm is circulated as a heat medium. Specifically, the fluid medium is first heated to about 1000 ° C. in the combustion furnace 112 and introduced into the medium separator 114 together with the combustion exhaust gas EX containing carbon dioxide (CO ₂ ). In the medium separator 114, the high-temperature fluid medium and the combustion exhaust gas EX are separated, and the separated high-temperature fluid medium is introduced into the gasification furnace 116. Then, the fluidized medium introduced into the gasification furnace 116 is fluidized into layers by a gasifying agent (steam, nitrogen, air, oxygen, inert gas, etc.) introduced from the bottom of the gasification furnace 116, and then finally Thus, it is returned to the combustion furnace 112. The combustion exhaust gas EX separated by the medium separation device 114 is recovered by the boiler 118 and then discharged to the outside.

  The gasification furnace 116 is, for example, a bubbling fluidized bed (bubbling fluidized bed) gasification furnace, and as a gasification raw material, for example, low-grade fuel such as lignite is gasified at 700 ° C. to 900 ° C. to generate synthesis gas X1. Generate. In the present embodiment, by supplying water vapor to the gasification furnace 116, the gasification raw material is gasified to generate the synthesis gas X1 (water vapor gasification).

  And since the synthesis gas X1 produced | generated in the gasification furnace 116 contains tar, water vapor | steam, etc., it is sent to the downstream synthesis gas purification apparatus 200, and is refine | purified.

(Syngas purification apparatus 200)
As shown in FIG. 1, the synthesis gas purification apparatus 200 includes a reforming furnace (oxidation reforming furnace) 210, a boiler 212, an oil scrubber 220, a mist separator 222, a sedimentation separation unit 230, and an oil delivery unit 240. And a water delivery unit 250. The reforming furnace 210, the oil scrubber 220, the mist separator 222, and the sedimentation separation unit 230 are all in a sealed structure together with the combustion furnace 112, the medium separation device 114, and the gasification furnace 116 described above. Is prevented from entering. Thereby, the purity fall of a synthesis gas can be suppressed.

  The reforming furnace 210 adds oxygen or air to the synthesis gas X1 produced in the gasification furnace 116 to raise the temperature of the product to about 900 to 1500 ° C., thereby reforming (oxidation reforming) the tar contained in the synthesis gas X1. The boiler 212 performs heat exchange between the synthesis gas X2 reformed in the reforming furnace 210 and steam, that is, recovers sensible heat of the synthesis gas X2 with steam, and sets the outlet temperature of the synthesis gas X2 to 300 ° C. to 600 ° C. Bring to ℃.

  The oil scrubber (oil cleaning unit) 220 sprays oil onto the synthesis gas X2, thereby bringing the synthesis gas X2 into contact with the oil and washing the synthesis gas X2 with oil. Since oil has a high affinity for tar, the oil scrubber 220 sprays oil onto the synthesis gas X2, so that the tar contained in the synthesis gas X2 is dissolved in the oil. Thereby, tar is removed from the synthesis gas X2, and synthesis gas X3 and the oil Y1 after washing | cleaning are produced | generated. Then, in the oil scrubber 220, the synthesis gas X3 washed with oil is sent to the mist separator 222, and after-washing oil (including tar, water, oil) Y1 that is the oil after washing the synthesis gas X2, It is sent to a sedimentation separation unit 230 described later.

  The mist separator (oil cleaning unit) 222 sprays oil onto the synthesis gas X3 to bring the synthesis gas X3 into contact with the oil and cleans the synthesis gas X3 with oil. The oil particle size sprayed by the mist separator 222 is smaller than the oil particle size sprayed by the oil scrubber 220. Thereby, in the oil scrubber 220, the mist-like tar contained in the synthesis gas X3 that could not be sufficiently separated and removed is removed from the synthesis gas X3, and the purified synthesis gas X4 and the washed oil Y2 are generated.

  In the present embodiment, the oil used in the oil scrubber 220 and the mist separator 222 is, for example, heavy oil, light oil, vegetable oil, or the like.

  Thus, the purified synthesis gas X4 is generated, and the washed oil (including tar, water, and oil) Y2, which is the oil after washing the synthesis gas X3 in the mist separator 222, is sent to the sedimentation separation unit 230 described later. The The temperature of the purified synthesis gas X4 and the temperatures of the washed oils Y1 and Y2 are maintained at about 250 ° C. to 550 ° C. without being cooled in the oil scrubber 220 and the mist separator 222.

  The sedimentation separation unit 230 stores the washed oil Y1 sent from the oil scrubber 220 and the washed oil Y2 sent from the mist separator 222, and separates the water Z2 from the washed oil Y1 and Y2 depending on the difference in specific gravity. . Note that the temperature in the sedimentation separation unit 230, that is, the temperature of the washed oils Y1 and Y2 in the sedimentation separation unit 230 is about 250 ° C to 550 ° C.

  The oil delivery unit 240 includes a pump, and sends out the washed oil Z1 (about 250 ° C. to 550 ° C.) from which the water Z2 has been separated in the sedimentation separation unit 230 to the combustion furnace 112 and the gasification furnace 116. The combustion furnace 112 uses the washed oil Z1 for heating the fluidized medium. More specifically, the combustion furnace 112 burns the washed oil Z1 as fuel and heats the fluidized medium. Further, the gasification furnace 116 gasifies the oil Z1 after cleaning as a gasification raw material.

  In this way, the oil delivery unit 240 sends the washed oil Z1 to the combustion furnace 112 and the gasification furnace 116, so that the washed oil (including oil and tar) Z1 is discarded or disposed of. No equipment is required. Conventionally, in the combustion furnace, coal is burned as fuel to heat the fluid medium, but the oil delivery unit 240 sends the washed oil Z1 to the combustion furnace 112 to replace the coal, or Since oil Z1 after washing can be used as fuel in addition to coal, the fuel cost for heating the fluidized medium can be reduced. Moreover, since the tar contained in the oil Z1 after washing can also be used as a fuel or a gasification raw material, tar that has been conventionally discarded can be effectively used.

  Further, since the oil delivery unit 240 sends the washed oil Z1 from which the water Z2 has been separated by the sedimentation separation unit 230 to the combustion furnace 112, it is possible to avoid a temperature drop of the combustion furnace 112 due to the water Z2. .

  Further, conventionally, the oil after washing has been cooled by a cooler in order to be reused for washing the synthesis gas. That is, the heat of the oil after washing was discarded in the cooler. However, the oil delivery unit 240 of this embodiment delivers the high-temperature after-cleaning oil Z1 of about 250 ° C. to 550 ° C. to the combustion furnace 112 and the gasification furnace 116 without cooling using a cooler or the like. Therefore, it can be efficiently used without throwing away the heat of the oil Z1 after washing.

  The water delivery unit 250 includes a pump, and sends out water (about 250 ° C. to 550 ° C.) Z2 separated from the oils Y1 and Y2 after washing in the sedimentation separation unit 230 to the gasification furnace 116. And the gasification furnace 116 uses the water Z2 sent out by the water sending part 250 for gasification of the gasification raw material.

  More specifically, as described above, the temperature of the fluidized medium in the gasification furnace 116 is about 700 ° C. to 900 ° C. For this reason, the water Z <b> 2 sent out by the water sending unit 250 becomes steam in the gasification furnace 116. And the gasification raw material will be gasified by this water vapor.

  In this way, the water delivery unit 250 sends out the water Z2 to the gasification furnace 116, thereby disposing the water (including a small amount of oil and tar) Z2 and a facility for performing processing for disposal. It becomes unnecessary. Moreover, the amount of water vapor | steam for gasifying the gasification raw material currently introduced conventionally can be reduced by the water delivery part 250 sending water Z2 to the gasification furnace 116. FIG. Therefore, it is possible to reduce the heat energy for generating water vapor.

  Furthermore, since the water delivery part 250 sends out the high temperature water Z2 about 250 to 550 degreeC to the gasification furnace 116, it can utilize efficiently, without throwing away the heat which water Z2 has.

(Syngas production method)
Next, a synthesis gas generation method using the synthesis gas generation system 100 will be described. FIG. 2 is a flowchart for explaining a process flow of the synthesis gas generation method according to the first embodiment. Here, the fluid medium circulates through the combustion furnace 112, the medium separator 114, and the gasification furnace 116. Moreover, in the gasification furnace 116, the fluidized medium is fluidized into a fluidized bed with water vapor (gasifying agent).

  As shown in FIG. 2, first, a gasification raw material is introduced into the gasification furnace 116, and synthesis gas X1 is generated (synthesis gas generation step S300). The generated synthesis gas X1 is oxidized and reformed into the synthesis gas X2 in the reforming furnace 210, and is cooled by the boiler 212 (oxidation reforming step S302).

  Subsequently, the synthesis gas X2 is introduced into the oil scrubber 220. In the oil scrubber 220, the synthesis gas X2 and oil are brought into contact with each other, thereby washing the synthesis gas X2 with the oil. The cleaned synthetic gas X3 is introduced into the mist separator 222, and the synthetic gas X3 and oil are brought into contact with each other in the mist separator 222, thereby cleaning the synthetic gas X3 with the oil (cleaning step S304). In this way, purified synthesis gas X4 is generated.

  On the other hand, the washed oil Y 1 generated in the oil scrubber 220 and the washed oil Y 2 generated in the mist separator 222 are sent to the sedimentation separation unit 230. In the sedimentation separation unit 230, the washed oils Y1 and Y2 are separated into the washed oil Z1 and the water Z2 (separation step S306).

  The washed oil Z1 separated in the sedimentation separation unit 230 is sent to the combustion furnace 112 and the gasification furnace 116 by the oil delivery unit 240 (oil delivery step S308). By doing so, in the combustion furnace 112, the washed oil Z1 is burned as fuel, and the fluid medium is heated. Further, in the gasification furnace 116, the washed oil Z1 is gasified as a gasification raw material, and a synthesis gas X1 is generated.

  On the other hand, the water Z2 separated in the sedimentation separation unit 230 is sent to the gasification furnace 116 by the water delivery unit 250 (water delivery step S310). By doing so, in the gasification furnace 116, the water Z2 becomes water vapor, and the gasification raw material is gasified as a part of the gasifying agent.

  As described above, according to the synthesis gas generation system 100 and the synthesis gas generation method using the same according to the present embodiment, the synthesis gas X2 and X3 are washed with oil having high affinity with tar, thereby synthesizing. Tar can be efficiently removed from the gases X2 and X3. Further, by introducing the washed oil Z1 into the combustion furnace 112 and the gasification furnace 116, it becomes possible to effectively use the discarded oil Z1 without discarding the thermal energy, and the removed tar is converted into fuel or gasification. It can be used effectively as a raw material.

  Conventionally, instead of the oil scrubber 220 and the mist separator 222, a spray tower and a mist separator for removing tar in the synthesis gas X2 and X3 by spraying water have been provided. The waste water treatment equipment for processing was needed. More specifically, the wastewater treatment facility is a pressurized flotation tank (or coagulation sedimentation treatment) that introduces pressurized air into the wastewater and floats and removes suspended solids contained in the wastewater, an ammonia diffusion tower By applying activated sludge (aerobic microorganisms) to the wastewater, it comprises an activated sludge tank that decomposes and removes organic substances contained in the wastewater, and a final sedimentation tank that separates the wastewater and solids.

  However, the synthesis gas generation system 100 according to the present embodiment uses an oil scrubber 220 for spraying oil instead of a spray tower for removing tar in the synthesis gas X2 and X3 by spraying water or a mist separator for spraying water. In addition, by providing the mist separator 222 for spraying oil, there is almost no drainage. Further, water Z2 contained in the synthesis gas X2 and X3 (water derived from water vapor in the gasification furnace 116) and contained in the oils Y1 and Y2 after being washed in the oil scrubber 220 and the mist separator 222. Are separated in the sedimentation separation unit 230 and sent (returned) to the gasification furnace 116 by the water delivery unit 250.

  Therefore, a large-scale wastewater treatment facility as described above is not necessary, and it is possible to reduce the place and cost required for the wastewater treatment facility. Furthermore, by introducing the water Z2 separated from the oils Y1 and Y2 after washing into the gasification furnace 116, the thermal energy of the water Z2 can be effectively used without being discarded.

(Second Embodiment: Syngas Generation System 400)
FIG. 3 is a diagram for explaining a synthesis gas generation system 400 according to the second embodiment. As shown in FIG. 3, the synthesis gas generation system 400 includes a synthesis gas generation device 410 and a synthesis gas purification device 420. In FIG. 3, the flow of gas (gas) is indicated by solid arrows, the flow of gasification raw materials is indicated by two-dot chain arrows, and the flow of liquids such as water and oil is indicated by white arrows.

  The synthesis gas generation system 400 includes a gasification furnace 416 and a heating unit 418.

  The gasification furnace 416 is, for example, a fluidized bed type gasification furnace or a moving bed type gasification furnace that forms a moving bed by flowing a fluid medium (sand) in the vertical downward direction under its own weight. The heating unit 418 is configured with, for example, an indirect heat exchanger, and heats the fluidized medium in the gasification furnace 416.

  The gasification furnace 416 gasifies a low-grade fuel such as lignite at 700 ° C. to 900 ° C. as a gasification raw material to generate synthesis gas. In this embodiment, by supplying water vapor to the gasification furnace 416, the gasification raw material is gasified to generate synthesis gas.

  And since the synthesis gas X1 produced | generated in the gasification furnace 416 contains tar, water vapor | steam, etc., it is sent to the downstream synthesis gas refiner | purifier 420 and refine | purified.

(Syngas purification apparatus 420)
As shown in FIG. 3, the syngas purification apparatus 420 includes a reforming furnace (oxidation reforming furnace) 210, a boiler 212, an oil scrubber 220, a mist separator 222, and an oil delivery unit 440. The The reforming furnace 210, the oil scrubber 220, and the mist separator 222, together with the gasification furnace 416 described above, all have a sealed structure, and prevent air from entering from the outside. Thereby, the purity fall of a synthesis gas can be suppressed.

  The reforming furnace 210, boiler 212, oil scrubber 220, and mist separator 222 have substantially the same functions as the reforming furnace 210, boiler 212, oil scrubber 220, and mist separator 222 of the first embodiment described above. The same reference numerals are assigned and duplicate descriptions are omitted, and here, the oil delivery section 440 having different functions will be described in detail.

  The oil delivery unit 440 sends the washed oil Y1 and Y2 to the gasification furnace 416. Thereby, in the gasification furnace 416, after-cleaning oil Y1 and Y2 can be gasified as a gasification raw material. The washed oils Y1 and Y2 contain water. By introducing this water into the gasification furnace 416, water vapor that has been conventionally introduced to gasify the gasification raw material is used. The amount can be reduced. Therefore, it is possible to reduce the heat energy for generating water vapor.

  Further, the oil delivery unit 440 delivers the high-temperature washed oils Y1 and Y2 such as about 250 ° C. to 550 ° C. to the gasification furnace 416, so that the heat of the washed oils Y1 and Y2 can be efficiently used without being discarded. be able to. Furthermore, it becomes possible to effectively use the removed tar as a gasification raw material.

(Syngas production method)
Next, a synthesis gas generation method using the synthesis gas generation system 400 will be described. FIG. 4 is a flowchart for explaining a process flow of the synthesis gas generation method according to the second embodiment. Here, steam (gasification agent) is introduced into the gasification furnace 416.

  The synthesis gas generation step S300, the oxidation reforming step S302, and the cleaning step S304 are substantially the same as the synthesis gas generation step S300, the oxidation reforming step S302, and the cleaning step S304 of the first embodiment described above. The same reference numerals are assigned and redundant description is omitted, and the oil delivery step S450 having a different process will be described in detail here.

  The post-cleaning oil Y1 generated in the oil scrubber 220 and the post-cleaning oil Y2 generated in the mist separator 222 are sent directly to the gasification furnace 416 by the oil delivery unit 440 (oil delivery step S450). By doing so, in the gasification furnace 416, the oils Y1 and Y2 after cleaning are gasified, and the water contained in the oils Y1 and Y2 after cleaning becomes water vapor, and as a part of the gasifying agent, gasified raw materials (such as lignite) Coal and oil Y1, Y2) after washing will be gasified.

  As described above, according to the synthesis gas generation system 400 and the synthesis gas generation method using the same according to the present embodiment, the synthesis gas X2 and X3 are washed with oil having high affinity with tar, thereby synthesizing. Tar can be efficiently removed from the gases X2 and X3. Further, by introducing the cleaned oils Y1 and Y2 into the gasification furnace 416, it is possible to effectively use the thermal energy of the cleaned oils Y1 and Y2 without being discarded. Furthermore, the removed tar can be effectively used as a gasification raw material.

  As mentioned above, although preferred embodiment of this invention was described referring an accompanying drawing, it cannot be overemphasized that this invention is not limited to this embodiment. It will be apparent to those skilled in the art that various changes and modifications can be made within the scope of the claims, and these are naturally within the technical scope of the present invention. Is done.

  For example, in the first embodiment described above, the configuration including the sedimentation separation unit 230 has been described as an example. However, the sedimentation separation unit 230 is not an essential configuration, and the oil delivery unit 240 includes the oils Y1 and Y2 after washing. May be sent directly to the combustion furnace 112 and the gasification furnace 116.

  Further, in the first embodiment described above, the oil sending unit 240 has been described with respect to the configuration in which the washed oil Z1 is sent to the combustion furnace 112 and the gasification furnace 116. However, the oil sending unit 240 is configured to send the washed oil Z1. It may be sent to only one of the combustion furnace 112 and the gasification furnace 116. When the sedimentation separation unit 230 is not provided, the oil delivery unit 240 may send the washed oil Y1 and Y2 directly to one of the combustion furnace 112 and the gasification furnace 116.

  In the second embodiment described above, the oil delivery unit 440 sends the washed oils Y1 and Y2 directly to the gasification furnace 416. However, the settling separation unit 230 is provided, and the washed oil Y1 and After Y2 is stored in the sedimentation separation unit 230, the oil delivery unit 440 may deliver the gas to the gasification furnace 416. In the second embodiment, when the sedimentation separation unit 230 is provided, the water delivery unit 250 may be provided together and the water delivery unit 250 may send the water Z2 to the gasification furnace 416.

  In the above-described embodiment, the oil scrubber 220 and the mist separator 222 have been described as examples of the oil cleaning unit, but the oil scrubber 220 and the mist separator 222 may be provided.

  Moreover, in embodiment mentioned above, although demonstrated taking the example of the structure provided with the reforming furnace 210 and the boiler 212, the reforming furnace 210 and the boiler 212 are not essential structures. For example, as shown in FIG. 5, the synthesis gas generation system 500 includes a synthesis gas generation device 110 and a synthesis gas purification device 520, and the synthesis gas purification device 520 includes an oil scrubber 220 and a mist separator 222. In addition, the sedimentation separation unit 230, the oil delivery unit 240, and the water delivery unit 250 may be included.

  When the reforming furnace 210 is not provided as in the synthesis gas generation system 500 illustrated in FIG. 5, the synthesis gas X <b> 1 introduced into the oil scrubber 220 contains a large amount of tar as compared with the configuration including the reforming furnace 210. It is. Therefore, after-cleaning oils Y1 and Y2 contain a lot of tar, and after-washing oil Z1 sent to combustion furnace 112 and gasification furnace 116 by oil sending part 240 contains a lot of tar. Become. Thereby, in the combustion furnace 112, the fuel cost for heating a fluidized medium can further be reduced.

  In the case where the boiler 212 is not provided, a heat exchanger (cooler) or a boiler may be provided at the subsequent stage of the mist separator 222 in accordance with the heat resistant temperature of the equipment using the purified synthesis gas X4. Furthermore, a spray tower for spraying water, a mist separator for spraying water, and a booster for boosting the purified synthesis gas X4 may be provided in the subsequent stage of the mist separator 222.

  Further, in the second embodiment described above, the configuration including the reforming furnace 210 and the boiler 212 has been described as an example, but the boiler 212 and the heating unit 418 may not be provided. In this case, since the outlet temperature of the reforming furnace 210 (the temperature of X1 downstream of the reforming furnace 210) is 1000 ° C. or higher, the oils Y1 and Y2 after cleaning recover the heat of about 1000 ° C. of the synthesis gas X1. can do. Therefore, the gasification furnace 416 can heat the fluid medium with the heat recovered by the oils Y1 and Y2 after cleaning without providing the heating unit 418.

  In addition, each process of the synthesis gas production | generation method of this specification does not necessarily need to process in time series along the order described as a flowchart.

  The present invention can be used in a synthesis gas generation system that generates synthesis gas and a synthesis gas generation method.

100, 400, 500 ... synthesis gas generation system 112 ... combustion furnace 116, 416 ... gasification furnace 220 ... oil scrubber (oil cleaning section)
222 ... Mist separator (oil cleaning part)
230 ... Sediment separation part 240, 440 ... Oil sending part 250 ... Water sending part

Claims (3)

A combustion furnace for heating the fluid medium;
A fluidized medium heated by the combustion furnace and water vapor are introduced to form a fluidized bed of the fluidized medium, and a gasification raw material is gasified with the heat of the fluidized bed and the water vapor to generate synthesis gas. A gasifier,
An oil cleaning section for cleaning the synthesis gas with the oil by bringing the generated synthesis gas into contact with the oil; and
A precipitating separation section for storing the oil after washing which is an oil after washing the synthesis gas in the oil washing section, and separating water from the oil after washing according to a difference in specific gravity;
An oil delivery section for delivering the washed oil from which the water has been separated by the settling separation section to the combustion furnace;
A water delivery section for delivering the water separated by the settling separation section to the gasification furnace;
With
The combustion furnace uses the post-cleaning oil for heating the fluid medium. The oil delivery section sends the washed oil to the gasification furnace,
The synthesis gas generation system according to claim 1, wherein the gasification furnace gasifies the washed oil as a gasification raw material. A combustion furnace for heating the fluidized medium, and the fluidized medium heated by the combustion furnace, is introduced and the water vapor, a fluidized layer of flowable medium is formed, gasified by heat and water vapor the fluidized layer has A gasification furnace that gasifies a raw material to generate a synthesis gas, and a synthesis gas generation method using the gasification furnace,
Cleaning the synthesis gas with the oil by contacting the generated synthesis gas with the oil;
Storing the washed oil, which is the oil after washing the synthesis gas, and separating water from the washed oil according to the difference in specific gravity;
Sending the washed oil from which water has been separated to one or both of the combustion furnace and the gasification furnace;
Sending the separated water to the gasifier;
A synthesis gas generation method comprising:

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