[go: up one dir, main page]

CN108675294A - A kind of production method of coaly activated carbon powder - Google Patents

A kind of production method of coaly activated carbon powder Download PDF

Info

Publication number
CN108675294A
CN108675294A CN201810173247.1A CN201810173247A CN108675294A CN 108675294 A CN108675294 A CN 108675294A CN 201810173247 A CN201810173247 A CN 201810173247A CN 108675294 A CN108675294 A CN 108675294A
Authority
CN
China
Prior art keywords
coal
ash
activated carbon
carbon powder
production method
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810173247.1A
Other languages
Chinese (zh)
Inventor
夏国春
刘永雄
孙红宇
谭健锋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi Fangcheng Port Huachen Mining Industry Co Ltd
MAOMING YUEQIAO GROUP MINING CO Ltd
Original Assignee
Guangxi Fangcheng Port Huachen Mining Industry Co Ltd
MAOMING YUEQIAO GROUP MINING CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guangxi Fangcheng Port Huachen Mining Industry Co Ltd, MAOMING YUEQIAO GROUP MINING CO Ltd filed Critical Guangxi Fangcheng Port Huachen Mining Industry Co Ltd
Priority to CN201810173247.1A priority Critical patent/CN108675294A/en
Publication of CN108675294A publication Critical patent/CN108675294A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • C01B32/312Preparation
    • C01B32/318Preparation characterised by the starting materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/10Solid density
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

A kind of production method of coaly activated carbon powder, this method carry out according to the following steps:Step 1:It controls reduction kiln metabituminous coal and volume ratio is added not less than 1 with ilmenite concentrate:1, high-temperature region temperature is not less than 1100 DEG C in reduction kiln, generates duff ash;Step 2:Duff ash is subjected to magnetic separation through 1000 1500GS magnetic separators of magnetic field intensity;Step 3:Duff ash after magnetic separation is crossed into the screening of 10 40 mesh screens, the coal grain on sieve removes heavier impurity waste through dry type jigging machine, obtains pure coal grain again;The lower coal ash of sieve is removed by wind-force powder concentrator than heavier impurity waste, obtains pure coal ash;Step 4:By pure coal grain and coal ash merga pass Raymond mill milling to get coal quality activated carbon powder;Wherein, rotary kiln production reduced ilmenite selects smart bituminous coal of the fixed carbon not less than 48%, fugitive constituent not less than 25%, ash content no more than 8% with bituminous coal.This method need not again individually be crushed raw coal, activation process, reduce energy consumption, saved coaly activated carbon production cost.

Description

一种煤质活性炭粉的生产方法A kind of production method of coal-based activated carbon powder

技术领域technical field

本发明涉及一种活性炭粉的生产方法,具体是一种利用回转窑生产还原钛铁矿产生的固体废物—细煤灰生产煤质活性炭粉的生产方法。The invention relates to a production method of activated carbon powder, in particular to a production method for producing coal-based activated carbon powder by using fine coal ash, the solid waste produced by reducing ilmenite in a rotary kiln.

背景技术Background technique

煤质活性炭是一种黑色多孔的固体炭质,活性炭内孔隙结构发达,具有较大的表面积,有很强的物理吸附性能,能吸附气体、液体或胶态固体。煤质活性炭是以优质原煤为原料,通过粉碎、成型活化生产而成。Coal-based activated carbon is a black porous solid carbon. The activated carbon has a well-developed pore structure, a large surface area, and strong physical adsorption properties. It can adsorb gases, liquids or colloidal solids. Coal-based activated carbon is produced from high-quality raw coal through crushing and molding activation.

煤质活性炭强度高对各种水中的有机质、游离氯以及空气中有害气体有极强的吸附能力,广泛用于环保行业污水治理及城市饮用水深度净化的优良吸附剂,也应用于脱除空气中细菌及毒害气体。Coal-based activated carbon has high strength and has a strong adsorption capacity for organic matter, free chlorine and harmful gases in the air. It is widely used as an excellent adsorbent for sewage treatment in environmental protection industries and deep purification of urban drinking water. It is also used to remove air. Bacteria and toxic gases.

回转窑生产还原钛铁矿是以烟煤为燃料,煤在生产过程中一方面作为加热燃料,另一方面作为还原剂产生CO使钛精矿还原成为还原钛铁矿。烟煤在生产过程中并未完全燃烧,经筛分后,粗的未完全燃烧煤粒返回循环使用,细的煤粒及粉状煤灰(统称为细煤灰)由于有一定热值,通常被运往制砖厂作为内燃剂使用。The production of reduced ilmenite by rotary kiln is based on bituminous coal. In the production process, coal is used as a heating fuel on the one hand, and on the other hand, it is used as a reducing agent to generate CO to reduce ilmenite concentrate to reduced ilmenite. The bituminous coal is not completely burned during the production process. After screening, the coarse incompletely burned coal particles are returned for recycling, and the fine coal particles and powdered coal ash (collectively referred to as fine coal ash) are usually used due to their certain calorific value. Shipped to the brick factory for use as an internal combustion agent.

发明内容Contents of the invention

本发明的目的在于提供一种煤质活性炭粉的生产方法,该方法不需要再单独对原煤进行破碎、活化处理,减少了能源消耗,节约了煤质活性炭生产成本。The purpose of the present invention is to provide a production method of coal-based activated carbon powder, which does not need to separately crush and activate raw coal, reduces energy consumption, and saves the production cost of coal-based activated carbon.

为实现上述的目的,本发明提供以下的技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种煤质活性炭粉的生产方法,该方法按以下步骤进行:A kind of production method of coal-based activated carbon powder, the method is carried out according to the following steps:

步骤1:控制还原窑中烟煤与钛精矿加入体积比不低于1:1,还原窑内高温区温度不低于1100℃,产生细煤灰;Step 1: Control the volume ratio of bituminous coal and titanium concentrate in the reduction kiln to not be lower than 1:1, and the temperature in the high temperature zone in the reduction kiln is not lower than 1100°C to produce fine coal ash;

步骤2:将细煤灰经磁场强度1000-1500GS磁选机进行磁选;Step 2: Carry out magnetic separation of the fine coal ash through a magnetic separator with a magnetic field strength of 1000-1500GS;

步骤3:将磁选后的细煤灰过10-40目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the fine coal ash after magnetic separation through a 10-40 mesh screen, and the coal particles on the sieve are then removed by a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve After the wind power separator removes relatively heavy impurities and wastes, pure coal ash is obtained;

步骤4:将纯净的煤粒和煤灰合并通过雷蒙磨磨粉,即得煤质活性碳粉;Step 4: Combine pure coal particles and coal ash through Raymond mill to obtain coal-based activated carbon powder;

其中,回转窑生产还原钛铁矿用烟煤选用固定碳不低于48%、挥发份不低于25%、灰分不大于8%的精烟煤。Among them, the bituminous coal used for the reduction of ilmenite in the rotary kiln is selected from clean bituminous coal with fixed carbon not less than 48%, volatile matter not less than 25%, and ash content not greater than 8%.

上述中,烟煤的固定碳为52-56%。Among the above, the fixed carbon of bituminous coal is 52-56%.

上述中,烟煤的挥发份为33-35%。Among the above, the volatile content of bituminous coal is 33-35%.

上述中,烟煤的灰分为7.0-8%。Among the above, the ash content of bituminous coal is 7.0-8%.

上述中,还原窑中烟煤与钛精矿加入的体积比为1-1.5:1。In the above, the volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1-1.5:1.

上述中,还原窑内高温区温度为1100-1120℃。Among the above, the temperature in the high temperature zone in the reduction kiln is 1100-1120°C.

本发明具有以下特点:The present invention has the following characteristics:

1、利用回转窑生产还原钛铁矿废弃的细煤灰生产煤质活性炭粉,不需要再单独对原煤进行破碎、活化处理,减少了能源消耗,节约了煤质活性炭生产成本。1. Using the rotary kiln to produce and reduce the waste fine coal ash of ilmenite to produce coal-based activated carbon powder does not need to separately crush and activate the raw coal, which reduces energy consumption and saves the production cost of coal-based activated carbon.

2、对还原钛铁矿生产产生的固废进行了有效综合利用,可以变废为宝,节约资源,同时保护了环境。2. Effective and comprehensive utilization of the solid waste produced in the production of reduced ilmenite can turn waste into treasure, save resources and protect the environment.

3、通过将粉煤灰综合加工成煤质活性炭粉,创造了较好的经济效益。3. Through the comprehensive processing of fly ash into coal-based activated carbon powder, better economic benefits have been created.

具体实施方式Detailed ways

实施例1Example 1

本实施例提供的回转窑生产还原钛铁矿用煤选用的烟煤技术指标为:固定炭:52%;挥发份34%;灰分:8%。The technical indicators of bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 52%; volatile matter: 34%; ash content: 8%.

步骤1:控制还原窑中烟煤与钛精矿加入体积比为1:1,还原窑内高温区温度1100℃,产生细煤灰。Step 1: Control the volume ratio of bituminous coal and titanium concentrate in the reduction kiln to 1:1, and the temperature in the high temperature zone in the reduction kiln is 1100°C to produce fine coal ash.

步骤2:将细煤灰通过磁场强度1000GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:5%,符合生产煤质活性炭的要求;Step 2: Carry out magnetic separation and separation of fine coal ash through a magnetic separator with a magnetic field strength of 1000GS to obtain non-magnetic fine coal ash. The ash content of the coal particles after inspection is: 5%, which meets the requirements for the production of coal-based activated carbon;

步骤3:将非磁性细煤灰通过30目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒,筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 30-mesh sieve. The coal particles on the screen are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles. The coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;

步骤4:将纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine pure coal particles and pure coal ash through a Raymond mill and sieve through a 200-mesh sieve to obtain coal-based activated carbon powder.

煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.

经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:

这种煤质活性炭粉符合制造净化水用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for water purification.

实施例2Example 2

本实施例提供的回转窑生产还原钛铁矿用煤选用的精烟煤技术指标为:固定炭:54%;挥发份33%;灰分:7.5%。The technical indicators of the clean bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 54%; volatile matter: 33%; ash content: 7.5%.

步骤1:还原窑中烟煤与钛精矿加入体积比为:1.2:1,还原窑内高温区温度1150℃,产生细煤灰。Step 1: The volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1.2:1, and the temperature in the high temperature zone in the reduction kiln is 1150°C to produce fine coal ash.

步骤2:将细煤灰通过磁场强度1300GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:3.3%,符合生产煤质活性炭的要求;Step 2: The fine coal ash is separated by magnetic separation through a magnetic separator with a magnetic field strength of 1300GS to obtain non-magnetic fine coal ash. The ash content of the coal particles is 3.3% after inspection, which meets the requirements for the production of coal-based activated carbon;

步骤3:将非磁性细煤灰通过40目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 40-mesh sieve, and the coal particles on the screen are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;

步骤4:将步骤3得到的纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine the pure coal particles and pure coal ash obtained in step 3 and pass them through a Raymond mill, and sieve them through a 200-mesh sieve to obtain coal-based activated carbon powder.

煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.

经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:

这种煤质活性炭粉符合制造空气净化用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for air purification.

实施例3Example 3

本实施例提供的回转窑生产还原钛铁矿用煤选用的精烟煤技术指标为:固定炭:56%;挥发份35%;灰分:7.0%。The technical indicators of the clean bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 56%; volatile matter: 35%; ash content: 7.0%.

步骤1:还原窑中烟煤与钛精矿加入体积比为:1.5:1,还原窑内高温区温度1200℃,得到细煤灰。Step 1: The volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1.5:1, and the temperature in the high temperature zone in the reduction kiln is 1200°C to obtain fine coal ash.

步骤2:将细煤灰通过磁场强度1500GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:4.0%,符合生产煤质活性炭的要求;Step 2: The fine coal ash is separated by magnetic separation through a magnetic separator with a magnetic field strength of 1500GS to obtain non-magnetic fine coal ash. The ash content of the coal particles after inspection is: 4.0%, which meets the requirements for the production of coal-based activated carbon;

步骤3:将非磁性细煤灰通过20目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 20-mesh sieve, and the coal particles on the sieve are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;

步骤4:将步骤3得到的纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine the pure coal particles and pure coal ash obtained in step 3 and pass them through a Raymond mill, and sieve them through a 200-mesh sieve to obtain coal-based activated carbon powder.

煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.

经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:

这种煤质活性炭粉符合制造载体用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for carriers.

Claims (6)

1. a kind of production method of coaly activated carbon powder, which is characterized in that this method carries out according to the following steps:
Step 1:It controls reduction kiln metabituminous coal and volume ratio is added not less than 1 with ilmenite concentrate:1, high-temperature region temperature is not low in reduction kiln In 1100 DEG C, duff ash is generated;
Step 2:Duff ash is subjected to magnetic separation through magnetic field intensity 1000-1500GS magnetic separators;
Step 3:Duff ash after magnetic separation is crossed into the screening of 10-40 mesh screens, the coal grain on sieve removes through dry type jigging machine heavier again Impurity waste, obtain pure coal grain;The lower coal ash of sieve is removed by wind-force powder concentrator than heavier impurity waste, is obtained pure Coal ash;
Step 4:By pure coal grain and coal ash merga pass Raymond mill milling to get coal quality activated carbon powder;
Wherein, rotary kiln production reduced ilmenite selects fixed carbon not less than 25%, ash content not less than 48%, fugitive constituent with bituminous coal Smart bituminous coal more than 8%.
2. a kind of production method of coaly activated carbon powder according to claim 1, which is characterized in that the fixed carbon of bituminous coal is 52-56%.
3. a kind of production method of coaly activated carbon powder according to claim 1, which is characterized in that the fugitive constituent of bituminous coal is 33-35%.
4. a kind of production method of coaly activated carbon powder according to claim 1, which is characterized in that cigarette pit ash is 7.0-8%.
5. a kind of production method of coaly activated carbon powder according to claim 1, which is characterized in that reduction kiln metabituminous coal with The volume ratio that ilmenite concentrate is added is 1-1.5:1.
6. a kind of production method of coaly activated carbon powder according to claim 1, which is characterized in that high-temperature region in reduction kiln Temperature is 1100-1120 DEG C.
CN201810173247.1A 2018-03-02 2018-03-02 A kind of production method of coaly activated carbon powder Pending CN108675294A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810173247.1A CN108675294A (en) 2018-03-02 2018-03-02 A kind of production method of coaly activated carbon powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810173247.1A CN108675294A (en) 2018-03-02 2018-03-02 A kind of production method of coaly activated carbon powder

Publications (1)

Publication Number Publication Date
CN108675294A true CN108675294A (en) 2018-10-19

Family

ID=63799271

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810173247.1A Pending CN108675294A (en) 2018-03-02 2018-03-02 A kind of production method of coaly activated carbon powder

Country Status (1)

Country Link
CN (1) CN108675294A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1557979A (en) * 2004-01-14 2004-12-29 茂名粤桥集团矿业有限公司 Technology for producing and reducing ilmenite using rotary kiln
CN104526189A (en) * 2014-12-19 2015-04-22 昆明理工大学 Method for reducing ilmenite through microwave composite reducing agents and preparing electrode coatings
WO2015061701A1 (en) * 2013-10-24 2015-04-30 Biogenic Reagent Ventures, Llc Methods and apparatus for producing activated carbon from biomass through carbonized ash intermediates
CN106587056A (en) * 2016-12-30 2017-04-26 中南大学 Method for preparing active carbon from carbocoal
CN106629712A (en) * 2016-12-30 2017-05-10 中南大学 Method for preparing activated carbon from mixture of coal and biomass

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1557979A (en) * 2004-01-14 2004-12-29 茂名粤桥集团矿业有限公司 Technology for producing and reducing ilmenite using rotary kiln
WO2015061701A1 (en) * 2013-10-24 2015-04-30 Biogenic Reagent Ventures, Llc Methods and apparatus for producing activated carbon from biomass through carbonized ash intermediates
CN104526189A (en) * 2014-12-19 2015-04-22 昆明理工大学 Method for reducing ilmenite through microwave composite reducing agents and preparing electrode coatings
CN106587056A (en) * 2016-12-30 2017-04-26 中南大学 Method for preparing active carbon from carbocoal
CN106629712A (en) * 2016-12-30 2017-05-10 中南大学 Method for preparing activated carbon from mixture of coal and biomass

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
侯景潇: "升温和恒温条件下钛铁矿直接还原动力学解析", 《第十七届(2013年)冶金反应工程学学术会议论文集》 *
孙康: "钛提取冶金物理化学", 《钛提取冶金物理化学 *
李德春译: "《硅酸盐工业机械装备 下册》", 30 June 1959 *
李瑛娟主编: "《炭素生产机械设备》", 30 September 2017 *
李贤国主编: "《跳汰选煤技术》", 30 September 2016 *
莫畏等: "《钛冶金(第2版)》", 30 June 1998, 冶金工业出版社 *

Similar Documents

Publication Publication Date Title
CN104084128B (en) Changing food waste waste residue modification active sludge carbon is utilized for what waste water processed
CN110652963A (en) A kind of lanthanum carbonate modified co-pyrolysis sludge biochar and its preparation method and application
CN104289182B (en) A Simple Method for Co-preparing Composite Adsorbent Material with Straw and Coal Gangue
CN103288116B (en) Method for preparing high-purity calcium hydroxide from carbide slag
CN104923153A (en) Preparation method for Canna biological carbon capable of simultaneously adsorbing ammonia nitrogen and cadmium
CN110586031A (en) Preparation method of modified sludge carbon material
CN108325738B (en) A kind of cascade recovery method of metal aluminum in aluminum ash
CN110773123A (en) Biochar/zeolite composite adsorbent material and preparation method thereof
CN110624506B (en) Method for preparing water purifying agent using coal gasification slag and obtained water purifying agent
CN104069814A (en) Method for preparing modified wood chip hydrothermal charcoal by adopting KOH
CN110698174A (en) A kind of light sludge ceramsite, its preparation method and application
CN105126760B (en) Poly- hole sorbing material of one heavy metal species and preparation method thereof
CN103480330B (en) Biomass-modified adsorbent for adsorbing coking wastewater, and preparation method and application thereof
CN106540659A (en) The preparation method of paper mill sludge biomass carbon and the method for removing 2,4 Dichlorophenols in waste water
CN109173999A (en) A kind of preparation method and applications of biology carbon microspheres
CN103182295B (en) Modified wood dust adsorbent for oil removal and preparation method for same
CN110252397A (en) A kind of biochar-based composite material and its preparation method and application
CN106111060A (en) A kind of modification biological carbon composite and preparation thereof and application
CN107552001A (en) A kind of preparation and application for being used for the new bio charcoal of hexavalent chromium removal in water body
CN112108118B (en) Fenton sludge and cellulose-based magnetic biomass charcoal and preparation method and application thereof
CN106140086A (en) A kind of preparation method and applications of porous biological carrier adsorbing material
CN108675294A (en) A kind of production method of coaly activated carbon powder
CN106166473B (en) A method for preparing adsorbent by using non-metallic separators in waste circuit boards
CN103127922B (en) A kind of production method of adsorbent
CN108126655A (en) A kind of preparation method of the Jujun grasses charcoal of iron oxide modified

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information
CB02 Change of applicant information

Address after: 525000 C-03, zone 2, Henan, southwest area, Maoming hi tech Zone, Maoming City, Guangdong Province

Applicant after: Guangdong Yueqiao New Material Technology Co.,Ltd.

Applicant after: Guangxi Yueqiao New Material Technology Co.,Ltd.

Address before: 22nd floor, Jiayan Yinghui international building, 111 Zhanqian 5th Road, Maoming, Guangdong 525000

Applicant before: MAOMING UBRIDGE GROUP MINERAL INDUSTRY Co.,Ltd.

Applicant before: GUANGXI FANGCHENGGANG HUACHEN MINING INDUSTRY Co.,Ltd.

Address after: 538001 Gongche Town, Gangkou District, Fangchenggang City, Guangxi Zhuang Autonomous Region

Applicant after: Guangxi Yueqiao New Material Technology Co.,Ltd.

Applicant after: Guangdong Yueqiao New Material Technology Co.,Ltd.

Address before: 525000 C-03, zone 2, Henan, southwest area, Maoming hi tech Zone, Maoming City, Guangdong Province

Applicant before: Guangdong Yueqiao New Material Technology Co.,Ltd.

Applicant before: Guangxi Yueqiao New Material Technology Co.,Ltd.

RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20181019