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Low-rank coal microbial stepwise degradation method

A low-rank coal and microbial technology, applied in the direction of microorganism-based methods, microorganisms, biochemical equipment and methods, etc., can solve the problems of harsh processing conditions, low thermal efficiency, low degradation rate, etc., to improve efficiency, avoid consumption, enhance Hydrophilic effect

Active Publication Date: 2019-06-14
SHANGLUO UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] (1) Low power generation efficiency; low-rank coal has the characteristics of low calorific value and high moisture, which leads to low thermal efficiency;
[0004] (2) The processing conditions are harsh; low-rank coal gasification, liquefaction, pyrolysis, coking and other processing methods generally require high temperature and high pressure, and have high requirements for equipment;
[0005] (3) High combustion pollution; low-rank coal contains high N, S, heavy metal elements, and ash content. In addition to carbon dioxide and hydrocarbons, low-rank coal will also generate a large amount of smoke, nitrogen oxides, and sulfur during combustion. Pollutants such as oxides and heavy metal compounds
Often a single strain cannot produce many coal-degrading active substances (enzymes, alkalis, chelating agents, surfactants, etc.) that degrade coal
At present, most researchers use a single strain of bacteria to degrade coal by microorganisms, so the degradation rate is often low. Corresponding to the large number of degradation active sites in the coal), but the bacteria does not necessarily have a high degradation rate for other coals with different structural functional groups, that is, the strain lacks universality

Method used

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  • Low-rank coal microbial stepwise degradation method
  • Low-rank coal microbial stepwise degradation method
  • Low-rank coal microbial stepwise degradation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0083] This embodiment includes the following steps:

[0084] Step 1: Pulverize Inner Mongolia Huolinhe lignite (HLH) and dry it at 100°C for 1 hour, then grind and sieve in turn to obtain Inner Mongolia Huolinhe lignite (HLH) coal powder with a particle size of -0.15mm+0.075mm ;

[0085] Step 2, using a rotating bed photochemical reactor to carry out photooxidative pretreatment to the Inner Mongolia Huolinhe lignite (HLH) coal powder obtained in step 1, to obtain photooxidized Inner Mongolia Huolinhe lignite (GHLH) coal powder; The treatment conditions are: the amount of coal added is 20g / L of Inner Mongolia Huolinhe lignite (HLH) pulverized coal added to the rotating bed photochemical reactor per unit volume, the ultraviolet light intensity is 150W, the rotation speed is 120r / min, the oxidation time is 42h, and oxygen The flow rate is 800mL / min, and the oxygen passing time per liter is 10min based on the volume of the rotating bed photochemical reactor before photooxidation...

Embodiment 2

[0105] This embodiment includes the following steps:

[0106] Step 1, pulverizing the Yunnan Zhaotong lignite (ZTH) and drying it at 100°C for 1 hour, and then successively grinding and sieving to obtain Yunnan Zhaotong lignite (ZTH) coal powder with a particle size of -0.15mm+0.075mm;

[0107] Step 2, using a rotating bed photochemical reactor to carry out photooxidative pretreatment to the Yunnan Zhaotong lignite (ZTH) pulverized coal obtained in step 1, to obtain photooxidized Yunnan Zhaotong lignite (GZTH) pulverized coal; the conditions of the photooxidative pretreatment are : The amount of coal added is 20g / L of Yunnan Zhaotong lignite (ZTH) pulverized coal mass added to the rotating bed photochemical reactor per unit volume, the ultraviolet light intensity is 150W, the rotating speed is 120r / min, the oxidation time is 42h, the oxygen flow rate is 800mL / min, and the light Before the oxidation pretreatment, the oxygen flow time per liter is 10min based on the volume of th...

Embodiment 3

[0127] This embodiment includes the following steps:

[0128] Step 1, pulverizing Shanxi Hunyuan lignite (HYH) and drying at 100° C. for 1 hour, and then successively grinding and sieving to obtain Shanxi Hunyuan lignite (HYH) coal powder with a particle size of -0.15mm+0.075mm;

[0129] Step 2, using a rotating bed photochemical reactor to carry out photooxidative pretreatment to the Shanxi Hunyuan lignite (HYH) coal powder obtained in step 1, to obtain photooxidized Shanxi Hunyuan lignite (GHYH) coal powder; the photooxidative pretreatment The conditions are: the amount of coal added is 20g / L of Shanxi Hunyuan lignite (HYH) pulverized coal added to the rotary bed photochemical reactor per unit volume, the ultraviolet light intensity is 150W, the rotation speed is 120r / min, the oxidation time is 42h, and the oxygen flow rate is 800mL / min. min, before photooxidation pretreatment, the oxygen passing time per liter is 10min based on the volume of the rotating bed photochemical r...

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Abstract

The invention discloses a low-rank coal microbial stepwise degradation method. The method comprises the following steps: I, making low-rank coal into coal powder; II, performing photooxidation on thecoal powder to obtain photooxidized coal powder; III, adding the photooxidized coal powder into a liquid culture medium inoculated with streptomyces viridosporous, and performing primary degradation;IV, adding primary degradation coal residues subjected to sterilization into a liquid culture medium inoculated with pseudomonas putida, and performing secondary degradation; and V, adding the secondary degradation coal residues subjected to sterilization into a liquid culture medium inoculated with phanerochaete chrysosporium, and performing tertiary degradation. According to the invention, the streptomyces viridosporous, the pseudomonas putida and the phanerochaete chrysosporium are adopted to stepwise degrade the low-rank coal sequentially; various active substances, such as alkali, enzymes, chelating agents and surfactants, generated by the metabolism of the three kinds of bacteria are respectively utilized; the synergistic effects are realized on different degradation activity pointsin a low-rank coal structure; the degradation rate of the low-rank coal is improved; and basic conditions are created for further clean and efficient utilization of the low-rank coal.

Description

technical field [0001] The invention belongs to the technical field of microbial conversion of coal, and in particular relates to a method for microbial graded degradation of low-rank coal. Background technique [0002] As we all know, coal is one of the most important energy sources. China's coal reserves rank third in the world, and its coal production and consumption have always ranked first in the world. In the process of coal mining and utilization, with the preemptive mining, processing and utilization of high-quality high-rank coal, the proportion of low-rank coal in coal reserves is increasing. At present, more than 50% of low-rank coal in my country is used for power generation, followed by coking, gasification, liquefaction, and direct combustion for heating. The following problems exist in the utilization process of the above-mentioned low-rank coal: [0003] (1) Low power generation efficiency; low-rank coal has the characteristics of low calorific value and hi...

Claims

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Application Information

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IPC IPC(8): C10G1/00C12P1/04C12P1/02C12R1/465C12R1/40C12R1/645
Inventor 李建涛刘向荣蔡会武杨再文赵顺省杨杰石晨康红丽
Owner SHANGLUO UNIV