Natural mineral-based catalyst and gasification method using the same

A technology of natural minerals and catalysts, applied in the field of fluidized bed gasification, to achieve the effect of easy separation and recovery, and improved gasification activity

Active Publication Date: 2018-11-16
SK INNOVATION CO LTD +1
View PDF12 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, as mentioned above, in the case of using an alkali metal salt as a catalyst, the gasification reaction needs to be performed at a low temperature, thus reducing CO 2 There is a limitation in discharge volume

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Natural mineral-based catalyst and gasification method using the same
  • Natural mineral-based catalyst and gasification method using the same
  • Natural mineral-based catalyst and gasification method using the same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0131] Manufacture of catalyst using natural zeolite (1)

[0132] As an aqueous Fe precursor solution, FeCl 2 4H 2 Fe of O (Sanden Pure Chemical Industries, Ltd. Iron (II) chloride tetrahydrate, 99%), and as the Mg precursor aqueous solution, prepared MgCl 2 ·6H 2 Mg of O (Magnesium chloride hexahydrate from Sanden Junyaku Co., Ltd., 98%).

[0133] Thereafter, as described above, 100 g of natural zeolite particles heat-treated at 350° C. were put into a 1-liter beaker, and then 125 g of the Fe precursor aqueous solution and 94 g of the Mg precursor aqueous solution were added thereto. The mixture was stirred at 75°C for 6 hours, filtered, and the filtrate was dried at 105°C, and then calcined in an air atmosphere at a temperature of 900°C to produce a gasification catalyst.

[0134] The composition of the catalyst was analyzed by ICP-OES (720ICP-OES from Agilent Technologies), and it was confirmed that it contained 20.5% by weight of MgO and 27.0% by weight of Fe 2 o 3...

Embodiment 2

[0136] Production of catalysts using dolomite

[0137] As an aqueous Fe precursor solution, FeCl 2 4H 2 Fe of O (Sanden Pure Chemical Industries, Ltd. Iron (II) chloride tetrahydrate, 99%), and KCl K (Sanden Pure Chemical Industries, Ltd. Potassium chloride, 99.5%).

[0138] Thereafter, 100 g of the calcined dolomite particles were put into a 1 L beaker, and then 125 g of the Fe precursor aqueous solution and 74 g of the K precursor aqueous solution were added thereto. The above-mentioned mixture was stirred at 75°C for 6 hours, filtered, and the obtained solid was dried at 105°C, and then calcined in an air atmosphere at a temperature of 950°C to produce a catalyst.

[0139] The composition of the catalyst was analyzed by ICP-OES (720ICP-OES from Agilent Technologies), and it was confirmed that it contained 24.0% by weight of MgO and 27.5% by weight of Fe 2 o 3 and 10.5% by weight of K 2 O.

Embodiment 3

[0141] Production of catalysts using eluate of natural zeolite and olivine

[0142] 100 g of the above-produced olivine particles were put into a 1 L beaker, 400 ml of 5N hydrochloric acid was added thereto, stirred at 90° C. for 3 hours, and the acid-treated mixture was filtered to separate and recover the eluate.

[0143] The contents of elements (ions) extracted from the recovered eluate sample (5 ml) are shown in Table 7 below.

[0144] 【Table 7】

[0145] element (ion)

Mg

Ca

Fe

Al

Si

Content (wt%)

0.60

0.01

0.21

0.03

0.51

[0146] 100 g of the natural zeolite particles produced above were put into a 1 L beaker, and then 200 ml of the eluate was added. Thereafter, the mixture was stirred at 75° C. for 6 hours, filtered, and the obtained solid matter was dried at 105° C., and then calcined in an air atmosphere at a temperature of 900° C. to produce a catalyst.

[0147] The composition of the catalyst was analyzed by...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
particle diameteraaaaaaaaaa
melting pointaaaaaaaaaa
melting pointaaaaaaaaaa
Login to view more

Abstract

Embodiments of the present invention provide a gasification catalyst that supports an active ingredient based on a natural mineral to have a specific composition range, and by applying the catalyst to a fluidized bed gasification reactor, not only the gasification activity is improved but also the catalyst is easily separated and recovered gasification method.

Description

technical field [0001] The present invention relates to a catalyst based on natural minerals and a gasification method using the catalyst. More specifically, the present invention relates to a gasification catalyst supporting an active ingredient based on a natural mineral to have a specific composition range and a fluidized bed gasification method using the catalyst. Background technique [0002] Recently, with the depletion of petroleum resources, there is a need for a method of producing high value-added chemical products by effectively utilizing coal, especially low-grade carbon, and for this reason, a representative gasification process has attracted attention. [0003] Generally, the gasification process refers to reacting carbonaceous raw materials such as coal and biomass under the condition of supplying a gasification agent (for example, oxygen, steam, carbon dioxide, or their mixture), thereby converting them into A range of processes for forming gases consisting ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/78C10J3/54
CPCY02P20/52
Inventor 沈显愍金容祐权泰玩金龙铨
Owner SK INNOVATION CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products