6m焦炉投产初期的热工管理

简要介绍焦化厂6m焦炉投产一年多以来的生产现状，整改措施和焦炉热工管理。     

Optimization of design and operating parameters in a pilot scale Jameson cell for slime coal cleaning

The Jameson flotation cell has been commonly used to treat a variety of ores (lead, zinc, copper etc.), coal and industrial minerals at commercial scale since 1989. It is especially known to be highly efficient at fine and ultrafine coal recovery. However, although the Jameson cell has quite a simple structure, it may be largely inefficient if the design and operating parameters chosen are not appropriate. In this study, the design and operating parameters of a pilot scale Jameson cell were optimized to obtain a desired metallurgical performance in the slime coal flotation. The optimized design parameters are the nozzle type, the height of the nozzle above the pulp level, the downcomer diameter and the immersion depth of the downcomer. Among the operating parameters optimized are the collector dosage, the frother dosage, the percentage of solids and the froth height. In the optimum conditions, a clean coal with an ash content of 14.90% was obtained from the sample slime having 45.30% ash with a combustible recovery of 74.20%. In addition, a new type nozzle was developed for the Jameson cell, which led to an increase of about 9% in the combustible recovery value.     

Kinetic Study on Absorption of SO2 and NOX with Acidic NaClO2 Solutions Using the Spraying Column

The operating conditions of this study are close to the typical operating conditions of flue gas desulfurization system in coal-fired power plants. The aim of this study is to investigate the absorption kinetics of SO2 and NO from simulated flue gas into an aqueous solution of acidic sodium chlorite using a bench-scale spraying column. The range of absorption rates measured in this study is between 1.91×10?11 and 9.59×10?10?mol?s?1?cm?2. The range of rate constants measured in this study is between 1.32×107 and 1.21×108?(L?mol?1)1.9?s?1, and the average rate constant is 6.16×107?(L?mol?1)1.9?s?1. The activation energy and frequency factor are 129 Kcal/mol (53.97 KJ/mol) and 6.93×1016?[(L/mol)1.9/s], respectively.     

煤层防塌钻井液技术

从煤层岩的强度等力学性能和化学结构、密度、亲油亲水性等理化性能综合分析了塔里木盆地依奇克里克区块煤层坍塌的机理，确定了防塌措施，用封堵实验法考查了粒径、温度、封堵剂种类与加量等因素对钻井液封堵防塌性能的影响，优选出的煤层防塌钻井液技术配方，在依西-1井、依南-4井等井的现场应用中取得了较好的煤层防塌效果，井径规则，起下钻，电测，取心，下套管，固井作业均顺利。     

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中国煤层气资源丰富 ,据估算 ,埋深 2 0 0 0m以浅的煤层气资源达 (30～ 35 )× 10 12 m3 。但中国煤层气地面开发刚进入起步阶段 ,加之中国煤田地质条件比较复杂 ,因此研究中国特殊地质条件下煤层气的解吸、扩散和渗流机理的具体地质表现是认识煤层气可采性的关键。针对我国煤层气开采的特殊性 ,我国采取“地面开采和井巷抽放相结合”的方针。然而井巷开采占了相当的比例。本文建立了煤层气扩散渗流数学物理方程 ,并对煤层气渗流偏微分方程 ,采用差分法 ,进行了数值模拟计算。模拟结果表明 ,所建立的煤层气扩散渗流模型较准确地反映了煤层中煤层气流动规律 ,模拟后的煤层气压力变化曲线可以确定煤层气的开采压力变化范围和煤层气产气最大面积 ,对我国大面积低渗透性无烟煤煤层气的开发具有指导意义。     

我国煤炭生产的环境问题及其对策研究

论文分析了我国煤炭生产中所存在的环境问题 ,并提出采取应用全面绿色管理、贯彻实施ISO14 0 0 0系列标准及推广应用清洁生产等对应措施和方法。其中全面绿色管理是作者首次提出的全新概念。     

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煤层气采出有扩散和渗流两个过程，比常规天然气层中的渗流方程复杂。煤层气由煤层流入井筒的过程为：随着煤层中水的不断采出，地层压力下降，吸附在煤层中的煤层气被解吸出来，并扩散至割理，割理中的气体渗流到达井筒。采用非平衡态吸附模型，研究单相煤层气在煤体和割理中的流动规律。在拟稳态流和不稳态流的数学模型假设下，用气体标准压力代替Ｌａｎｇｍｕｉｒ吸附公式中的压力，得到气层中标准压力所满足的方程。如果考虑无限大地层或有界圆形封闭和定压地层，最终得到井底无量纲准压力及其导数的解。     

煤气发生炉自动控制系统设计

介绍了煤气发生系统的组成和工作流程,进一步分析了系统的功能和输入输出需求.在控制系统总体结构设计和硬件设计的基础上,详细论述了自动加煤和自动除灰的程序流程设计.实际应用表明了该控制系统设计的合理性.     

准噶尔盆地白家海地区侏罗系聚煤作用与层序地层

煤层在层序划分与对比中具有十分重要的参考意义。以准噶尔盆地白家海地区侏罗系为例，通过对该地区几个聚煤时期的碎屑物质的供应程度、古地貌格局、湖平面变化（基准面变化）、气候及古植物等内在与外在因素的分析，并结合侏罗系高分辨率层序地层研究，认为该地区侏罗系煤层受多种因素控制，并主要发育于基准面稳定上升的早期，且与层序的时空演化存在着有机联系。     

THE EFFECT OF TEMPERATURE TREATMENT ON PENETRANT TRANSPORT IN COAL

The macromolecular structure of coals thermally treated at 35^°C, 100^°C and 150^°C was investigated by dynamic penetrant transport in thin coal sections. The effects of temperature, carbon content in coal, and penetrant type on the transport mechanism were investigated. Dynamic swelling studies showed that penetrant transport into coal is a function of the average molecular weight between crosslinks, M_c. The penetrant transport mechanism at low activity is Fickian diffusion. The transport mechanism deviates from Fickian diffusion to anomalous transport, when the carbon content in coal and penetrant activity increase. Variations of the diffusion coefficients and relaxation constants were determined using a diffusion/relaxation coupled model.