CN114195148B - 一种烟气脱硫脱硝用高强度活性焦的制备方法 - Google Patents

一种烟气脱硫脱硝用高强度活性焦的制备方法 Download PDF

Info

Publication number
CN114195148B
CN114195148B CN202111546034.7A CN202111546034A CN114195148B CN 114195148 B CN114195148 B CN 114195148B CN 202111546034 A CN202111546034 A CN 202111546034A CN 114195148 B CN114195148 B CN 114195148B
Authority
CN
China
Prior art keywords
coal
active coke
strength
coke
preparation
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.)
Active
Application number
CN202111546034.7A
Other languages
English (en)
Other versions
CN114195148A (zh
Inventor
熊银伍
梁大明
孙仲超
白效言
李小亮
盛明
解炜
吴涛
李艳芳
李光华
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.)
CCTEG China Coal Research Institute
Original Assignee
CCTEG China Coal Research Institute
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 CCTEG China Coal Research Institute filed Critical CCTEG China Coal Research Institute
Priority to CN202111546034.7A priority Critical patent/CN114195148B/zh
Publication of CN114195148A publication Critical patent/CN114195148A/zh
Application granted granted Critical
Publication of CN114195148B publication Critical patent/CN114195148B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • C01B32/33Preparation characterised by the starting materials from distillation residues of coal or petroleum; from petroleum acid sludge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • 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
    • 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
    • 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
    • C01B32/354After-treatment
    • C01B32/36Reactivation or regeneration
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/08Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form in the form of briquettes, lumps and the like
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
    • C10B57/045Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing mineral oils, bitumen, tar or the like or mixtures thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/08Non-mechanical pretreatment of the charge, e.g. desulfurization
    • C10B57/10Drying
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/102Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/30Sulfur compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/40Nitrogen compounds
    • B01D2257/404Nitrogen oxides other than dinitrogen oxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4806Sorbents characterised by the starting material used for their preparation the starting material being of inorganic character
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

本发明公开了一种高强度活性焦的制备方法。该包括如下步骤:先将原料煤进行磨粉,再将得到的煤粉按一定的粒度配比,加入黏结剂进行搅拌成型;成型后的物料通过干燥、炭化和活化后即得所述活性焦成品。本发明提供的高强度活性焦产品具有如下优点:(1)本发明的方法可用于无烟煤或烟煤为主的原料,原料来源广泛。(2)通过控制煤粉粒度级配方法、原料配方,以及炭活化条件可制备出性能优异的产品。(3)高强度活性焦产品的耐压强度可达90daN,远远高于国家标准和市售的活性焦产品。

Description

一种烟气脱硫脱硝用高强度活性焦的制备方法
技术领域
本发明属于活性炭生产技术领域,具体涉及一种烟气脱硫脱硝用高强度活性焦的制备方法。
背景技术
活性焦烟气净化技术自2005年推广以来,完成了从单一的脱硫向多污染物联合脱除的技术和装备升级,取得了较大的技术进步和发展。该技术具有一材多用、一体化工业装置设计、无二次污染和可满足超低排放等优点,目前全国建设活性焦干法烟气净化装置近百套,活性焦材料的年消费量也达到35万吨以上,相比于2015年增长600%,广泛分布在有色冶炼、燃煤锅炉、钢铁、焦化等多个国民经济主导产业领域。
目前国内制备活性焦通常采用的工序是:1、磨粉,将原料煤经磨粉机进行磨粉;2、压条成型,将煤粉、煤焦油(或黏结剂)和少量水搅拌、混合、压条成型;3、炭化,将成型料炭化;4、活化,将炭化料加入斯列普炉进行活化;5、包装,采用包装机对成品进行包装。
活性焦的制备方法和工艺对活性焦的工业应用性能指标影响较大,检测方法一般按照GB/T 30202-2013执行。由于活性焦脱硫脱硝技术采用移动床结构,活性焦在移动过程中会造成磨碎破碎,而破碎量会影响装置的稳定运行,必须通过筛分机筛除,并适当补充新鲜活性焦。如果活性焦的机械强度足够高,移动过程中活性焦的破碎料越少,补充的新鲜活性焦量越少,运行成本越低。国标规定的活性焦强度为37daN以上。
本发明制备的活性焦在耐压强度上具有特色,最高可达100daN以上,耐磨最高可达99%,通过查阅一种用于烟气净化高性能活性焦的制备方法(中国,申请号:CN202110614975.3)专利,该专利制备的活性焦耐压强度50~52daN之间,耐磨强度97.3~98.1之间,本发明耐压强度远远高于该文献专利的结果,耐磨强度也大于该文献专利的结果。
发明内容
本发明的目的是提供一种制备高强度活性焦的方法。
本发明所提供的高强度活性焦的方法,包括如下步骤:
先将原料煤进行磨粉,将煤粉按一定的粒度配比,加入黏结剂进行搅拌成型;成型后的物料通过干燥、炭化和活化后即可得到高耐压强度的活性焦成品。
所述原料煤为无烟煤和/或烟煤、焦煤、兰炭,配置质量比为(5-6):(1-3):(1-3),具体可为5:3:2,5:2:3或6:2:2等。
所述煤粉粒度为200目和325目,两者的质量比为(5~9):(5~1),具体可为5:5,6:4或9:1。
所述黏结剂为煤焦油,添加量为煤粉质量的20%~30%,具体可为:20%,25%和30%;
所述煤焦油中加入煤粉量的2%~20%的煤沥青进行煤焦油的沥青含量调配,具体可为:2%,10%、15%和20%;
所述煤沥青还可以与原料煤直接磨粉,磨粉至325~200目,无需加入到煤焦油中,所述煤沥青加入量可为煤粉量的2%~20%,具体可为:2%、10%、15%和20%;
所述干燥温度为80~120℃,具体可为80℃、100℃和120℃,干燥时长0.5~2h,具体可为0.5、1h和2h;
所述炭化终温为550~700℃,具体可为550℃、600℃、650℃和700℃,升温速率为5~8℃/min,具体可为5℃/min、6℃/min和8℃/min;
所述活化温度为850~950℃,具体可为850℃、900℃和950℃;活化时间为30~50min,具体可为30min,40min和50min。
利用上述方法制备得到的高强度的活性焦产品也属于本发明的保护范围。
上述方法制备的活性焦耐压强度达90daN以上。
本发明提供的高强度活性焦产品具有如下优点:
(1)本发明的方法可用于无烟煤或烟煤为主的原料,原料来源广泛。
(2)通过控制煤粉粒度级配方法、原料配方,以及炭活化条件可制备出性能优异的产品。
(3)高强度活性焦产品的耐压强度可达90daN,远远高于国家标准和市售的活性焦产品。
具体实施方式
下面结合具体实施例对本发明作进一步阐述,但本发明并不限于以下实施例。所述方法如无特别说明均为常规方法。所述原材料如无特别说明均能从公开商业途径获得。
活性焦耐压强度和耐磨强度依据GB/T 33202.3-2013进行检测,由于本方法的活性焦耐压强度较高,如依据原标准不足以体现本方法制备的活性焦的耐压强度好,对标准中的耐压强度计数方法进行了调整,将原标准规定大于50daN的数值以50daN计,改为大于50daN的数值以实际数值计。
实施例1、高强度活性焦的制备
(1)先将无烟煤、焦煤、兰炭以5:3:2的质量配比混合,然后加入原煤质量10%的煤沥青后进行磨粉,分别制成200目和325目两种不同粒度,然后将200目和325目煤粉按9:1质量配比混合,加入占比煤粉质量30%的煤焦油作为黏结剂利用捏合机对原料进行混合,所有原料充分混合后利用四柱液压机对物料进行Φ9mm柱状成型;
(2)将成型的物料在100℃温度下干燥1h;
(3)将干燥后的物料进行炭化,将物料的炭化终温设定为700℃,物料升温速率控制在5℃/min;
(4)将炭化料进行活化,活化温度设定为900℃,活化时间为40min。
本实施实例制备的活性焦耐压强度为97daN,耐磨强度98.8%。
实施例2、高强度活性焦的制备
(1)先将烟煤、焦煤、兰炭以6:2:2的质量配比混合,然后加入原煤量的15%煤沥青后进行磨粉,分别制成200目和325目两种不同粒度,然后将200目和325目煤粉按5:5质量配比混合,加入占比煤粉量25%的煤焦油作为黏结剂利用捏合机对原料进行混合,所有原料充分混合后利用四柱液压机对物料进行Φ9mm柱状成型;
(2)将成型的物料在120℃温度下干燥0.5h;
(3)将干燥后的物料进行炭化,将物料的炭化终温设定为700℃,物料升温速率控制在8℃/min;
(4)将炭化料进行活化,活化温度设定为850℃,活化时间为50min。
本实施实例制备的活性焦耐压强度为98daN,耐磨强度98.9%。
实施例3、高强度活性焦的制备
(1)先将无烟煤、焦煤、兰炭以5:2:3的质量配比混合,然后加入原煤质量20%的煤沥青后进行磨粉,分别制成200目和325目两种不同粒度,然后将200目和325目煤粉按6:4质量配比混合,加入占比煤粉量20%的煤焦油作为黏结剂利用捏合机对原料进行混合,所有原料充分混合后利用四柱液压机对物料进行Φ9mm柱状成型;
(2)将成型的物料在100℃温度下干燥1h;
(3)将干燥后的物料进行炭化,将物料的炭化终温设定为650℃,物料升温速率控制在6℃/min;
(4)将炭化料进行活化,活化温度设定为950℃,活化时间为30min。
本实施实例制备的活性焦耐压强度为100daN,耐磨强度99%。
对比例1、活性焦的制备
(1)先将无烟煤、焦煤、兰炭以5:2:3的质量配比混合,制成200目的煤粉,加入占比煤粉量20%的煤焦油作为黏结剂利用捏合机对原料进行混合,所有原料充分混合后利用四柱液压机对物料进行Φ9mm柱状成型;
(2)将成型的物料在100℃温度下干燥1h;
(3)将干燥后的物料进行炭化,将物料的炭化终温设定为650℃,物料升温速率控制在6℃/min;
(4)将炭化料进行活化,活化温度设定为900℃,活化时间为30min。
本对比例制备的活性焦耐压强度为58daN,耐磨强度97.1%。
对比例2、活性焦的制备
(1)先将烟煤、焦煤、兰炭以2:2:6的质量配比混合,制成200目的煤粉粒度,加入占比煤粉量25%的煤焦油作为黏结剂利用捏合机对原料进行混合,所有原料充分混合后利用四柱液压机对物料进行Φ9mm柱状成型;
(2)将成型的物料在120℃温度下干燥0.5h;
(3)将干燥后的物料进行炭化,将物料的炭化终温设定为650℃,物料升温速率控制在5℃/min;
(4)将炭化料进行活化,活化温度设定为900℃,活化时间为25min。
本对比例制备的活性焦耐压强度为63daN,耐磨强度97.2%。

Claims (5)

1.一种高强度活性焦的制备方法,包括如下步骤:
先将原料煤进行磨粉,再将得到的煤粉按一定的粒度配比,加入黏结剂进行搅拌成型;成型后的物料通过干燥、炭化和活化后即得所述活性焦成品;
所述原料煤由无烟煤或烟煤、焦煤和兰炭组成,质量比为(5-6):(1-3):(1-3);
所述煤粉的粒度为200目和325目,两者的质量比为(5~9):(5~1);
所述黏结剂为煤焦油,其添加量为所述煤粉质量的20%~30%;
所述制备方法中还加入煤沥青;所述煤沥青的加入方式为:所述煤沥青与所述原料煤直接磨粉,磨粉至325~200目,所述煤沥青加入量为所述原料煤质量的2%~20%。
2.根据权利要求1所述的制备方法,其特征在于:
所述干燥温度为80~120℃,干燥时长0.5~2h。
3.根据权利要求1所述的制备方法,其特征在于:所述炭化终温为550~700℃,升温速率为5~8℃/min。
4.根据权利要求1所述的制备方法,其特征在于:所述活化温度为850~950℃,活化时间为30~50min。
5.权利要求1-4中任一项所述方法制备得到的活性焦。
CN202111546034.7A 2021-12-16 2021-12-16 一种烟气脱硫脱硝用高强度活性焦的制备方法 Active CN114195148B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111546034.7A CN114195148B (zh) 2021-12-16 2021-12-16 一种烟气脱硫脱硝用高强度活性焦的制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111546034.7A CN114195148B (zh) 2021-12-16 2021-12-16 一种烟气脱硫脱硝用高强度活性焦的制备方法

Publications (2)

Publication Number Publication Date
CN114195148A CN114195148A (zh) 2022-03-18
CN114195148B true CN114195148B (zh) 2023-03-21

Family

ID=80654662

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111546034.7A Active CN114195148B (zh) 2021-12-16 2021-12-16 一种烟气脱硫脱硝用高强度活性焦的制备方法

Country Status (1)

Country Link
CN (1) CN114195148B (zh)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101147847A (zh) * 2007-07-24 2008-03-26 天津工业大学 中间相炭微球基管式炭膜及其制备方法
CN107892299A (zh) * 2017-12-19 2018-04-10 胡光远 一种活性焦吸附剂的制备方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4018391A1 (de) * 1990-06-08 1991-12-12 Saar Kokerei Gmbh Verfahren zum erzeugen von aktivkoks
JPH10296078A (ja) * 1997-04-23 1998-11-10 Nippon Steel Corp 高強度、高吸着能を有する活性コークスの製造方法
CN101485972B (zh) * 2009-01-20 2012-02-15 北京国电清新环保技术股份有限公司 煤基脱硫用活性焦及其制备方法
CN103738960A (zh) * 2013-12-17 2014-04-23 中国矿业大学 一种提高压块活性炭强度的颗粒级配配煤法
CN112479206A (zh) * 2020-11-20 2021-03-12 中冶南方都市环保工程技术股份有限公司 一种用于烟气净化高性能活性焦的制备方法

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101147847A (zh) * 2007-07-24 2008-03-26 天津工业大学 中间相炭微球基管式炭膜及其制备方法
CN107892299A (zh) * 2017-12-19 2018-04-10 胡光远 一种活性焦吸附剂的制备方法

Also Published As

Publication number Publication date
CN114195148A (zh) 2022-03-18

Similar Documents

Publication Publication Date Title
CN114180572B (zh) 烟气脱硫脱硝用高强度活性焦的制备方法
CN109621893B (zh) 一种利用化工含碳废料制备活性焦的方法
CN105062583A (zh) 一种干燥煤粉与半焦配合制备气化水煤浆的方法
CN109970378A (zh) 基于协同理论及碳化/高温技术的固废基胶凝材料制备工艺
CN103992807B (zh) 大型捣固煤饼在焦炉上生产气化用炭化型煤/焦的方法
CN104342552B (zh) 一种用于冶金球团的复合粘合剂及其生产方法
CN103626471A (zh) 一种利用磷尾矿和磷渣生产的蒸养砖及其制备方法
CN109384225B (zh) 一种生产脱硫脱硝活性炭的方法
CN101864333A (zh) 钢铁厂专用高效活性粘结剂
CN103803552B (zh) 一种工业硅冶炼还原剂的制备方法
CN110316734A (zh) 一种工业硅生产用碳质还原剂球团及其制备方法
CN103585956A (zh) 一种磁性木质素基活性炭的制备方法
CN109652156A (zh) 型煤粘结剂、生物质型煤及其制备方法
CN102557034B (zh) 用于生产工业硅的还原剂
CN111847409A (zh) 一种利用磷矿粉生产磷矿粉球的方法
CN111518973A (zh) 一种用于炼钢高炉喷吹原料的多元混合兰炭焦粉
CN107400743B (zh) 一种以兰炭作为部分燃料的高炉喷煤方法
CN114195148B (zh) 一种烟气脱硫脱硝用高强度活性焦的制备方法
CN113735631A (zh) 一种低能耗钾钙镁磷肥的生产方法
CN109384228B (zh) 一种脱硫脱硝活性炭及其制备方法
CN102230077B (zh) 一种利用混合料生产烧结矿的方法
CN114959259B (zh) 钠盐在通过腐植酸粘结剂制备铁矿球团的方法中作为分散剂的应用
CN111663035A (zh) 一种烧结用复合含碳块的使用方法
CN111517324A (zh) 一种制备活性炭的方法
KR20030052954A (ko) 제철공정용 성형탄과 그 제조방법

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
GR01 Patent grant
GR01 Patent grant