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公开(公告)号：US20160355742A1
公开(公告)日：2016-12-08
申请号：US15038801
申请日：2014-11-21
Applicant: ChangZheng Engineering Co., Ltd.
Inventor： Congbin Jiang , Wei Xin , Honghai Li , Ruiheng Gao , Yongjin Chen , Xiaofei Li , Yan Zhang , Li Zhang
CPC classification number: C10J3/86 , C01B3/02 , C01B3/50 , C01B2203/04 , C01B2203/0877 , C10J3/485 , C10J3/506 , C10J3/84 , C10J2300/093 , C10J2300/0976 , C10J2300/1853
Abstract: A carbonaceous substance dry powder gasification device and method, the device comprising from bottom to top a lower cooling and purification section (1), a gasification reaction section (2), a cooling reaction section (3) and an upper cooling and purification section (4); an initial cooling device is disposed at the connection between the cooling reaction section and the gasification reaction section; and a plurality of nozzles are circumferentially arranged in the gasification reaction section. The method comprises: a gasification reaction is conducted between a carbonaceous substance and an oxygenated gasifying agent to generate crude synthesis gas and ash; part of the crude synthesis gas and most of the ash go downstream for cooling and gasification, and the cooled and ash removed crude synthesis gas is transferred to subsequent processes, and the quenched ash is discharged through an ash outlet; the remaining crude synthesis gas and fly ash go upstream to mix with a cooling substance for cooling, and then are transferred to the cooling reaction section for reacting with the incompletely reacted carbon and added gasification agent; the crude synthesis gas and the fly ash are cooled and purified to remove the fly ash, and the clean low-temperature crude synthesis gas is transferred to subsequent processes. The method avoids ash blocking at an ash outlet in an upstream air-exhaust method, and also avoids overheating at the top in a downstream air-exhaust method, thus improving the carbon conversion rate.
Abstract translation: 一种含碳物质干粉气化装置及其制造方法，其特征在于，从底部至顶部包括下部冷却和净化部分（1），气化反应部分（2），冷却反应部分（3）和上部冷却和净化部分 4）; 初始冷却装置设置在冷却反应部和气化反应部之间的连接处; 在气化反应部中周向配置多个喷嘴。 该方法包括：在碳质物质和含氧气化剂之间进行气化反应，产生粗合成气和灰分; 粗合成气的一部分和大部分灰分下游进行冷却和气化，将冷却和除灰的粗合成气转移到随后的过程中，淬火灰通过灰分出口排出; 剩余的粗合成气和飞灰上游与冷却物质混合冷却，然后转移到冷却反应段，与不完全反应的碳和添加的气化剂反应; 将粗合成气和飞灰冷却并纯化以除去飞灰，并将干净的低温粗合成气转移到随后的工艺中。 该方法避免了上游排气法灰渣的灰渣堵塞，同时也避免了下游排气法顶部过热，提高了碳转化率。
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公开(公告)号：US09926502B2
公开(公告)日：2018-03-27
申请号：US15038792
申请日：2014-11-21
Applicant: ChangZheng Engineering Co., Ltd.
Inventor： Wei Xin , Honghai Li , Ruiheng Gao , Yongjin Chen , Xiaofei Li , Pin Liu , Lizhi Li
CPC classification number: C10J3/84 , C01B3/02 , C10J3/485 , C10J3/845 , C10J2300/093 , C10J2300/0959 , C10J2300/1631 , C10J2300/1807 , C10J2300/1846
Abstract: A carbonaceous substance powder gasification system and gasification method. The system comprises a carbonaceous substance reaction apparatus and a gas return apparatus used for raising the pressure of some of a raw syngas cooled and preliminarily purified downstream of the reaction apparatus, then blending with high-temperature raw syngas upstream of the reaction apparatus and reducing the temperature. The method comprises reacting in a gasification reaction apparatus the carbonaceous substance and a gasification agent to generate raw syngas and ash and slag, some of the high-temperature raw syngas moving downstream with fly ash and liquid slag, and some of the high-temperature syngas moving upstream with fly ash; the downstream part of the high-temperature raw syngas being cooled, preliminarily purified and deslagged, then pressurized, and the wet raw syngas being injected into the system and blended with the upstream high-temperature raw syngas; the remainder of the high-temperature syngas moving upstream with fly ash and blending and cooling with the low-temperature wet syngas injected by the preliminary cooler, and optionally being entered into the cooling reaction stage; the cooled or cooling-reacted raw syngas continuing upstream, passing through the upper cooling stage and cooling again and ash being removed to obtain the raw syngas.
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公开(公告)号：US09809771B2
公开(公告)日：2017-11-07
申请号：US15038801
申请日：2014-11-21
Applicant: ChangZheng Engineering Co., Ltd.
Inventor： Congbin Jiang , Wei Xin , Honghai Li , Ruiheng Gao , Yongjin Chen , Xiaofei Li , Yan Zhang , Li Zhang
CPC classification number: C10J3/86 , C01B3/02 , C01B3/50 , C01B2203/04 , C01B2203/0877 , C10J3/485 , C10J3/506 , C10J3/84 , C10J2300/093 , C10J2300/0976 , C10J2300/1853
Abstract: A carbonaceous substance dry powder gasification device and method, the device comprising from bottom to top a lower cooling and purification section (1), a gasification reaction section (2), a cooling reaction section (3) and an upper cooling and purification section (4); an initial cooling device is disposed at the connection between the cooling reaction section and the gasification reaction section; and a plurality of nozzles are circumferentially arranged in the gasification reaction section. The method comprises: a gasification reaction is conducted between a carbonaceous substance and an oxygenated gasifying agent to generate crude synthesis gas and ash; part of the crude synthesis gas and most of the ash go downstream for cooling and gasification, and the cooled and ash removed crude synthesis gas is transferred to subsequent processes, and the quenched ash is discharged through an ash outlet; the remaining crude synthesis gas and fly ash go upstream to mix with a cooling substance for cooling, and then are transferred to the cooling reaction section for reacting with the incompletely reacted carbon and added gasification agent; the crude synthesis gas and the fly ash are cooled and purified to remove the fly ash, and the clean low-temperature crude synthesis gas is transferred to subsequent processes. The method avoids ash blocking at an ash outlet in an upstream air-exhaust method, and also avoids overheating at the top in a downstream air-exhaust method, thus improving the carbon conversion rate.
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公开(公告)号：US20170037330A1
公开(公告)日：2017-02-09
申请号：US15038792
申请日：2014-11-21
Applicant: CHANGZHENG ENGINEERING CO., LTD.
Inventor： Wei Xin , Honghai Li , Ruiheng Gao , Yongjin Chen , Xiaofei Li , Pin Liu , Lizhi Li
CPC classification number: C10J3/84 , C01B3/02 , C10J3/485 , C10J3/845 , C10J2300/093 , C10J2300/0959 , C10J2300/1631 , C10J2300/1807 , C10J2300/1846
Abstract: A carbonaceous substance powder gasification system and gasification method. The system comprises a carbonaceous substance reaction apparatus and a gas return apparatus used for raising the pressure of some of a raw syngas cooled and preliminarily purified downstream of the reaction apparatus, then blending with high-temperature raw syngas upstream of the reaction apparatus and reducing the temperature. The method comprises reacting in a gasification reaction apparatus the carbonaceous substance and a gasification agent to generate raw syngas and ash and slag, some of the high-temperature raw syngas moving downstream with fly ash and liquid slag, and some of the high-temperature syngas moving upstream with fly ash; the downstream part of the high-temperature raw syngas being cooled, preliminarily purified and deslagged, then pressurized, and the wet raw syngas being injected into the system and blended with the upstream high-temperature raw syngas; the remainder of the high-temperature syngas moving upstream with fly ash and blending and cooling with the low-temperature wet syngas injected by the preliminary cooler, and optionally being entered into the cooling reaction stage; the cooled or cooling-reacted raw syngas continuing upstream, passing through the upper cooling stage and cooling again and ash being removed to obtain the raw syngas.
Abstract translation: 一种含碳物质粉末气化系统和气化方法。 该系统包括碳质物质反应装置和气体回收装置，用于提高反应装置下游冷却和预净化的一些原始合成气的压力，然后与反应装置上游的高温原料合成气共混并减少 温度。 该方法包括在气化反应装置中使碳质物质与气化剂反应生成原料合成气，灰渣和渣，一些高温原料合成气在飞灰和液渣下游运动，一些高温合成气 用飞灰向上游移动; 将高温原料合成气的下游部分冷却，预先净化并脱盐，然后加压，将湿原料合成气注入系统并与上游高温原料合成气混合; 剩余的高温合成气用飞灰向上游移动，并通过预备冷却器注入的低温湿合成气进行混合和冷却，并任选进入冷却反应阶段; 冷却或冷却反应的原料合成气继续上游，通过上部冷却阶段并再次冷却，灰分被除去以获得原始合成气。
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