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Gasifier and operating method of gasifier

A technology of gasifier and oxidant, applied in fixed bed gasification and other directions

Active Publication Date: 2021-02-02
YANMAR POWER TECHNOLOGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] In this way, in conventional gasifiers, when oxidizing raw materials containing silica and potassium (such as rice husks) to generate gaseous products, in order to suppress both the generation of tar and the generation of crystalline silica , requires pretreatment, or divides the oxidation into multiple stages (for example, perform primary oxidation at a temperature of 700°C to 800°C, and then perform secondary oxidation on only the gasified gas at a temperature above 1000°C), Alternatively, tar (such as the tar produced by oxidizing the raw material at a temperature of 700°C to 800°C) or crystalline silica (such as the crystalline silica produced by oxidizing the raw material at a temperature of 1000°C or higher) is removed in post-treatment. Such a multi-stage process is not a structure that can simultaneously suppress both the generation of tar oil and the generation of crystalline silica.

Method used

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  • Gasifier and operating method of gasifier
  • Gasifier and operating method of gasifier
  • Gasifier and operating method of gasifier

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0197] Next, the following reference Figure 7 to Figure 13 Another embodiment (Example 1) of the gasifier 102 according to this embodiment will be described.

[0198] Figure 7 to Figure 13 It is a schematic diagram schematically showing another embodiment of the gasifier 102 according to this embodiment. Figure 7 to Figure 13 Gasifiers 1021A to 1021G according to the first to seventh embodiments of Example 1 are shown, respectively. in, Figure 7 to Figure 13 In , illustration of the control device 102g and the like is omitted.

[0199] exist Figure 7 to Figure 13 In the shown gasifiers 1021A to 1021G, for substantially figure 2 The structure of the gasifier 102 shown is the same and the same reference numerals are attached to the same structure, and the description thereof is omitted.

no. 1 approach

[0201] Figure 7 The gasification furnace 1021A according to the first embodiment shown is a gasification furnace in which char R is deposited to form a char layer δ (specifically, a char deposition layer), and the generated fuel gas G flows upward. gasifiers (so-called fixed-bed up-suction gasifiers).

[0202] For the gasifier 1021A, in figure 2 In the gasifier 102 shown, the raw material introduction part 102a is provided above the uppermost part δxa of the assumed char layer δx, and the oxidant introduction part 102d is provided above the uppermost part δxa of the assumed char layer δx , and lower than the opening 102ah of the raw material introduction part 102a.

[0203] In addition, the opening 102dh of the oxidizing agent introduction portion 102d is formed such that the introduction direction of the oxidizing agent H is along the horizontal direction or upward (for example, obliquely upward) compared to the horizontal direction. The fuel gas outflow portion 102e is ...

no. 2 approach

[0209] for Figure 8 In the gasification furnace 1021B according to the second embodiment shown, Figure 7 In addition to the shown gasification furnace 1021A, at least one (in this example, both) of an endothermic reaction agent introduction part 102i and a heat capacity agent introduction part 102j is provided.

[0210] The gasification furnace 1021B further includes: an endothermic reactant introduction part 102i for introducing an endothermic reactant M; and a heat capacity agent introduction part 102j for a heat capacity agent N to be introduced. The gasification furnace 1021B may include either one of the endothermic reaction agent introduction part 102i and the heat capacity agent introduction part 102j.

[0211] At least one (in this example, both) of the endothermic reaction agent introduction part 102i and the heat capacity agent introduction part 102j is provided at a position facing the imaginary char layer δx of the furnace 102b. In this example, both the endoth...

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Abstract

A gasifier that oxidizes a raw material to generate a gaseous product is provided with a unit for maintaining the temperature of the oxidation zone where the raw material is oxidized at a predetermined predetermined temperature or a predetermined temperature range, and is provided with a unit for maintaining the raw material at a predetermined predetermined temperature The cells passed from the oxidized region in the time frame. A method of operating a gasifier for oxidizing raw materials to generate gaseous products, maintaining the temperature of the oxidation zone where the raw materials are oxidized at a predetermined predetermined temperature or within a predetermined temperature range, and maintaining the raw materials within a predetermined predetermined time range Pass through the oxidized area.

Description

technical field [0001] The present invention relates to a gasification furnace for oxidizing raw materials such as biomass to generate gas products, and a method for operating the gasification furnace. Background technique [0002] In a gasifier that oxidizes raw materials such as biomass to generate gas products, the raw materials are thermally decomposed to generate gas products (for example, carbon monoxide and hydrogen). In the process of producing such a gaseous product, generally, the raw material is carbonized, the carbonized char (carbonized product) is combusted, and the ash generated by the combustion is discharged to the outside. At this time, raw materials are introduced together with an oxidizing agent such as air, and the furnace is heated from the outside. [0003] In addition, in such a gasifier, tar is generated during the production of gaseous products. That is, the generated gas product contains a tar component. For example, when a gas product is combus...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10J3/02
CPCC10J3/02
Inventor 胁坂裕昭松本健
Owner YANMAR POWER TECHNOLOGY CO LTD