公开(公告)号：US20160257887A1

公开(公告)日：2016-09-08

申请号：US15033769

申请日：2014-11-26

Applicant: KABUSHIKI KAISHA KOBE SEIKO SHO (KOBE STEEL, LTD.)

Inventor： Maki HAMAGUCHI ,  Shohei WADA

IPC: C10B57/04 ,  C10L5/04 ,  C10B47/30 ,  C10B57/08 ,  C10B47/10 ,  C10L9/06 ,  C10B53/04

CPC classification number: C10B57/04 ,  C10B47/10 ,  C10B47/30 ,  C10B53/04 ,  C10B53/08 ,  C10B57/08 ,  C10L5/04 ,  C10L9/06 ,  C10L9/08 ,  C10L2290/02 ,  C10L2290/06 ,  C10L2290/24

Abstract: A method for producing a coke includes performing dry distillation of a mixture. The mixture includes: an ashless coal; an oxidized ashless coal obtained by an oxidation treatment of an ashless coal; and a raw petroleum coke. Relative to 100 parts by mass of a total of the ashless coal, the oxidized ashless coal and the raw petroleum coke, a content of the ashless coal is from 5 to 40 parts by mass, and a total content of the ashless coal and the oxidized ashless coal is from 30 to 70 parts by mass.

Abstract translation: 焦炭的制造方法包括进行混合物的干馏。 混合物包括：无灰煤; 通过无灰煤的氧化处理获得的氧化无灰煤; 和原料石油焦炭。 相对于100质量份的无灰煤，氧化无灰煤和原料石油焦炭，无灰煤的含量为5〜40质量份，无灰煤和氧化物的总含量 无灰煤为30〜70质量份。

公开(公告)号：US20150047961A1

公开(公告)日：2015-02-19

申请号：US14351745

申请日：2012-10-11

Applicant: JFE STEEL CORPORATION

Inventor： Kiyoshi Fukada ,  Hiroyuki Sumi ,  Izumi Shimoyama ,  Takashi Anyashiki ,  Hidekazu Fujimoto ,  Tetsuya Yamamoto ,  Yusuke Dohi

IPC: C01B31/02

CPC classification number: C01B31/02 ,  C01B32/05 ,  C10B53/04 ,  C10B53/08 ,  C10B57/04 ,  C10B57/08 ,  C10L5/363 ,  C10L5/366

Abstract: Coke is manufactured by blending two or more kinds of coal to form a coal blend and by carbonizing the coal blend. Interfacial tension among coal kinds is used as a control index for determining the blending ratio of each coal when forming the coal blend. It is possible to increase the strength of coke without increasing the material cost of a coal blend.

Abstract translation: 焦炭是通过混合两种或更多种煤来形成煤混合物并通过碳化煤混合物制造的。 煤种间的界面张力作为控制指标，用于确定形成煤混合物时每种煤的混合比例。 可以在不增加煤混合物的材料成本的情况下增加焦炭的强度。

公开(公告)号：US08936738B2

公开(公告)日：2015-01-20

申请号：US12670403

申请日：2008-07-21

Applicant: Qihui Lian

Inventor： Qihui Lian

IPC: B09B3/00 ,  C04B33/132 ,  C04B33/135 ,  C04B35/626 ,  C10B53/00 ,  C10B53/08 ,  C10L5/36 ,  C10L5/46 ,  C10L9/08 ,  B03B9/06 ,  C04B18/04

CPC classification number: B09B3/0025 ,  C04B18/04 ,  C04B33/1328 ,  C04B33/135 ,  C04B35/6267 ,  C10B53/00 ,  C10B53/08 ,  C10L5/361 ,  C10L5/363 ,  C10L5/46 ,  C10L9/083 ,  Y02E50/10 ,  Y02E50/15 ,  Y02E50/30 ,  Y02P40/69 ,  Y10S264/911 ,  Y10S264/915

Abstract: A disposal method for entirely recycling solid refuse includes the following steps: sorting, crushing, drying, pressing with high pressure to shaped articles, producing charcoal from combustible refuse in high temperature and firing incombustible refuse in high temperature, at last cooling high temperature articles to obtain solid fuel with various shapes and bricks or board used for building. The method achieves entirely recycling house refuse, especial solid refuse. The method recycles solid refuse to obtain fuel and building material with economic value. The method is simple and its processing cost is low.

Abstract translation: 完全回收固体垃圾的处理方法包括以下步骤：高压分选，粉碎，干燥，高压压制成型制品，高温可燃垃圾生产木炭，高温烧制不可燃垃圾，最后冷却高温物品 获得用于建筑物的各种形状和砖块或板材的固体燃料。 该方法完全可以回收垃圾，特别是垃圾。 该方法循环利用固体废物获得具有经济价值的燃料和建筑材料。 该方法简单，处理成本低。

公开(公告)号：US20130062185A1

公开(公告)日：2013-03-14

申请号：US13640696

申请日：2011-03-07

Applicant: Qin Xu ,  Congjun Wang

Inventor： Qin Xu ,  Congjun Wang

IPC: C10B7/00 ,  C10B57/04 ,  C10B53/08

CPC classification number: C10B47/46 ,  C10B7/14 ,  C10B53/08 ,  Y02P20/129

Abstract: The invention refers to a tunnel typed coking furnace with a movable sliding bed and the method using the same belonging to the coking field, comprising a furnace body (48), a front sealing door (7), a back sealing door (25), a branch flue (10), a bottom flue (12) and a main flue (6), comprising a first preparation chamber (3) for coaling, a preheating segment (50), a carbonization segment (51), a coke dry quenching segment (52), and a second preparation chamber (23) for coke outlet; each part has different formation from the others, and are interconnected in series with the others; the sliding bed (37) for coaling and tamping coal material (44) passes through the abovementioned five segment in series in order to coke. The invention may realize a production coal material with fixed formation through formation process with pressure, so as to obtain the coke product with the same and big size, in addition to high strength, high utilization rate of heat energy, high degree of mechanization, and it also may realize the clean exhaustion of flue, so as to be able to protect the environment and water resource, and realize clean production.

Abstract translation: 本发明涉及一种具有可移动滑动床的隧道式焦化炉及其使用方法，包括炉体（48），前密封门（7），后密封门（25）， 分支烟道（10），底部烟道（12）和主烟道（6），包括用于堆肥的第一制备室（3），预热段（50），碳化段（51），焦炭干燥淬火 段（52）和用于焦炭出口的第二制备室（23） 每个部分与其他部分不同，与其他部分相互串联; 用于烧结和捣碎煤材料（44）的滑动床（37）通过上述五个片段串联以便焦化。 本发明除了具有高强度，高能量利用率，高机械化能力以外，还可以通过形成压力实现具有固定形成的生产煤材料，以获得大小相同和大的焦炭产品 也可以实现烟道清洁耗尽，从而能够保护环境和水资源，实现清洁生产。

公开(公告)号：US20120204678A1

公开(公告)日：2012-08-16

申请号：US13389494

申请日：2010-07-28

Applicant: Takeshi Sato ,  Tetsuya Yamamoto ,  Hidekazu Fujimoto ,  Takashi Anyashiki

Inventor： Takeshi Sato ,  Tetsuya Yamamoto ,  Hidekazu Fujimoto ,  Takashi Anyashiki

IPC: C22B1/02 ,  F27D3/00

CPC classification number: C10B57/06 ,  C10B49/06 ,  C10B53/08

Abstract: Carbon iron composite is produced by feeding a formed product of a carbon-containing substance and an iron-containing substance into a carbonization furnace, carbonizing the formed product in a carbonization zone, blowing a coolant gas into the furnace through a coolant-gas-blowing tuyere disposed in a cooling zone to cool carbon iron composite, exhausting a furnace gas through an outlet in a top portion, and discharging the carbon iron composite through a lower portion of the cooling zone.

Abstract translation: 碳化铁复合体通过将含碳物质和含铁物质的成形物质进料到碳化炉中，在碳化区域中碳化碳化物，将冷却剂气体通过冷却气体吹入炉内 设置在冷却区中的风口冷却碳铁复合物，通过顶部的出口排出炉气，并通过冷却区的下部排出碳铁复合物。

公开(公告)号：US20120061618A1

公开(公告)日：2012-03-15

申请号：US13199814

申请日：2011-09-09

Applicant: James Santoianni ,  Pieter VanNierop ,  Michael Erskine Heier ,  Aleksandr Gorodetsky ,  Stephanie Reese ,  Kent Olis Hicks

Inventor： James Santoianni ,  Pieter VanNierop ,  Michael Erskine Heier ,  Aleksandr Gorodetsky ,  Stephanie Reese ,  Kent Olis Hicks

IPC: C01B3/24 ,  C22B5/00 ,  C22B1/00 ,  B01J19/08 ,  B28B1/14

CPC classification number: C04B14/022 ,  C04B7/02 ,  C04B12/04 ,  C04B28/04 ,  C04B35/62204 ,  C04B2111/00474 ,  C10B53/08 ,  C10J3/02 ,  C10J3/18 ,  C10J3/20 ,  C10J3/34 ,  C10J3/72 ,  C10J3/82 ,  C10J2200/06 ,  C10J2200/15 ,  C10J2300/092 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0983 ,  C10J2300/0993 ,  C10J2300/0996 ,  C10J2300/1238 ,  Y02W30/92 ,  C04B14/06 ,  C04B14/104 ,  C04B14/28 ,  C04B14/303 ,  C04B14/34 ,  C04B18/08

Abstract: A carbonaceous bed in a reactor includes carbon bearing material that is not coke and rather includes natural wood blocks or bricks formed of non-coke carbonaceous material in a binder along with, as options, other constituents such as catalysts and fluxing agents. The bed reduces the amount of coke required in processes such as for syngas production. Such non-coke units are applicable to an original carbonaceous bed in a reactor and also to replenishment of reacted carbon in the original bed. The bed may include ungasified carbon particulate matter separated from gaseous reaction products of a gasification reactor, either in non-coke bricks or otherwise applied, as may other carbonaceous material often regarded as waste such as spent potliner material from aluminum making and soot residue from a gasification reactor. Certain reactor structural modifications can also result in reduced consumption of carbon in a bed.

Abstract translation: 反应器中的含碳床包括不是焦炭的碳承载材料，而是包括粘合剂中由非焦炭碳质材料形成的天然木块或砖，以及其它成分如催化剂和助熔剂。 该床减少了合成气生产过程中所需的焦炭量。 这样的非焦炭单元适用于反应器中的原始碳质床，并且还可以补充原始床中反应的碳。 床可以包括与气化反应器的气态反应产物分离的非气化碳颗粒物质，无论是在非焦炭砖中，还是以其他方式施加，其他碳质材料通常被认为是废物，例如来自铝制造的废弃废料，以及来自 气化反应器。 某些反应器结构改性也可导致床中碳的消耗降低。

公开(公告)号：US20080190753A1

公开(公告)日：2008-08-14

申请号：US11884184

申请日：2006-05-12

Applicant: Kenji Katou ,  Isao Sugiyama ,  Yoshiaki Nakashima ,  Hiroshi Uematsu ,  Takashi Arima ,  Masahiko Yokomizo ,  Michitaka Sakaida

Inventor： Kenji Katou ,  Isao Sugiyama ,  Yoshiaki Nakashima ,  Hiroshi Uematsu ,  Takashi Arima ,  Masahiko Yokomizo ,  Michitaka Sakaida

IPC: C10B53/04

CPC classification number: C10B53/08 ,  C10B57/04 ,  C10B57/06 ,  C10B57/10 ,  C21B5/007

Abstract: A method of production of blast furnace coke comprising drying mixed coal, then, or simultaneously with the drying, classifying it to fine-grained coal and coarse-grained coal, then adding to the fine-grained coal at a temperature of 80 to 350° C. a caking additive comprised of one or more of a heavy distillate of tar, soft pitch, and petroleum pitch, agglomerating it by hot pressing, then mixing the clumps of coal and the coarse-grained coal and charging and carbonizing the mixture in a coke oven.

Abstract translation: 一种生产高炉焦炭的方法，包括将混合煤干燥，然后或同时进行干燥，将其分选成细粒度煤和粗粒煤，然后在80〜350℃的温度下加入细粒煤中 C.由一种或多种重质焦油，软沥青和石油沥青馏分组成的结块添加剂，通过热压将其凝聚，然后混合煤块和粗粒煤，并将混合物加入和碳化 焦炉

公开(公告)号：US20070014713A1

公开(公告)日：2007-01-18

申请号：US11525592

申请日：2006-09-22

Applicant: Fred Beierle

Inventor： Fred Beierle

IPC: C01B31/02

CPC classification number: C10B49/04 ,  C10B49/06 ,  C10B53/02 ,  C10B53/08 ,  C10L5/44 ,  F02B43/08 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/30

Abstract: The invention provides a process for the production of charcoal, fuel gas, and potassium from a biomass gassifier.

Abstract translation: 本发明提供从生物质放气器生产木炭，燃料气体和钾的方法。

公开(公告)号：US4388152A

公开(公告)日：1983-06-14

申请号：US341381

申请日：1982-01-21

Applicant: George E. Wasson ,  Frank W. Theodore ,  Lyndon D. Boyer ,  Matthew C. Sooter

Inventor： George E. Wasson ,  Frank W. Theodore ,  Lyndon D. Boyer ,  Matthew C. Sooter

IPC: C10B49/06 ,  C10B53/08 ,  C10B55/00 ,  C10B55/06 ,  C10B57/02

CPC classification number: C10B55/00 ,  C10B49/06 ,  C10B53/08

Abstract: A process for producing a distillable hydrocarbonaceous stream, fuel gases and blast furnace grade coke from a heavy, high sulfur, crude oil by producing delayed coke from at least a portion of the crude oil; crushing at least a portion of the coke to provide a finely divided coke feedstock to a briquetting operation where the finely divided coke is briquetted using crude oil or topped crude oil as a binder to produce briquettes of a size from about 3/4 inch to about 3 inches with the resulting briquettes being passed to a high temperature vertical calciner where the solids are desulfurized to produce a strong blast furnace grade coke. The distillable stream and fuel gas stream are recovered from the delayed coking operation, the vertical calciner and optionally a crude oil topping operation. In some instances coke particles in the size range from about 3/4 inch to about 3 inches may be passed directly to the calciner without crushing and briquetting. However, it is preferred to crush and briquette substantially all of the coke.

Abstract translation: 一种通过从至少一部分原油生产延迟焦炭来生产来自重质，高硫原油的可蒸馏烃物流，燃料气体和高炉级焦炭的方法; 粉碎至少一部分焦炭以提供细碎的焦炭原料至压块操作，其中使用原油或顶部原油作为粘合剂将细碎的焦炭压块，以产生尺寸为约3/4英寸至约 3英寸，所得到的团块被传递到高温垂直煅烧炉，其中固体被脱硫以产生强烈的高炉级焦炭。 从延迟焦化操作，垂直煅烧炉和任选的原油上料操作中回收可馏出的料流和燃料气体流。 在一些情况下，尺寸范围为约3/4英寸至约3英寸的焦炭颗粒可以直接通过煅烧炉而不破碎和压块。 然而，优选地粉碎和压块基本上所有的焦炭。

公开(公告)号：US4352720A

公开(公告)日：1982-10-05

申请号：US201262

申请日：1980-10-27

Applicant: Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs ,  Klaus Urbye

Inventor： Heinrich Weber ,  Kurt Lorenz ,  Horst Dungs ,  Klaus Urbye

IPC: C10B53/08 ,  C10B1/04

CPC classification number: C10B53/08 ,  Y02P20/129

Abstract: The process for the production of molded metallurgical coke from dried coal or fine coal mixtures with a low swelling index particularly highly volatile fine coal comprises mixing normal washed fine coal or fine coal mixtures of a grain size of from 0 to 10 mm and a swelling index of not more than 5 with a binder, pressing the mixture into briquettes, oxidizing the briquettes in a continuous material flow stream, and coking the oxidized briquettes continuously in an oven chamber by supplying indirectly and exhausting the coke oven gases with a temperature of 300.degree. to 1200.degree. C. The device for carrying out the process includes a vertically extending reactor housing having an oxidation chamber adjacent the top thereof with an indirectly heated vertical coking chamber directly below the oxidation chamber and with a cooling chamber directly below the coking chamber and including means for circulating heating gases into the coking chamber and then upwardly through the coking chamber and out adjacent the top of the coking chamber and into the oxidation chamber.

Abstract translation: 从干燥煤或具有低膨胀率特别是高挥发性细煤的细煤混合物生产成型冶金焦的方法包括混合正常洗涤的细煤或0至10mm的粒度的细煤混合物和溶胀指数 不超过5的粘合剂，将混合物压成团块，以连续的材料流动流将煤块氧化，并在室温炉中连续地将氧化的团块进行间歇加热并排出温度为300°C的焦化炉气体 用于进行该方法的装置包括垂直延伸的反应器壳体，其具有邻近其顶部的氧化室，其具有在氧化室正下方的间接加热的垂直焦化室，以及直接在焦化室下方的冷却室，并且包括 将加热气体循环进入焦化室，然后向上通过焦化室的装置 离开焦化室的顶部并进入氧化室。