节流式差压流量计的发展和现状

文章介绍节流式差压流量计的特点及标准化进程，煤气流量测量中存在的难点以及正在试图解决的途径。     

煤气设施防腐实践及影响质量因素分析

根据近几年三明钢铁公司煤气设施的防腐实践，就影响煤气设施的质量因素进行了分析。     

提高热采注汽系统热效率的研究

为了降低热采成本和提高经济效益 ,建立了热采注汽系统热效率的数学模型。根据实测数据计算了 9个注汽系统的热效率。提出了改进注汽系统热效率的行之有效的措施。根据排烟的氧含量的大小 ,可以确定注汽锅炉热效率改进程度 ;按管线允许热损失量和保温材料种类 ,设计保温层厚度 ,可大大提高输汽管线热效率。仅此两项 ,即可使大部分注汽系统热效率提高 7%以上 ,井底蒸汽干度提高 10 %以上。     

KINETICS OF HYDROCARBON GAS GENERATION FROM MARINE KEROGEN AND OIL: IMPLICATIONS FOR THE ORIGIN OF NATURAL GASES IN THE HETIANHE GASFIELD, TARIM BASIN, NW CHINA

In this paper we derive kinetic parameters for the generation of gaseous hydrocarbons (C_1‐5) and methane (C₁) from closed‐system laboratory pyrolysis of selected samples of marine kerogen and oil from the SW Tarim Basin. The activation energy distributions for the generation of both C_1‐5 (Ea = 59‐72kcal, A = 1.0×10¹⁴ s^?1) and C₁ (Ea = 61‐78kcal, A = 6.06×10¹⁴ s^?1) hydrocarbons from the marine oil are narrower than those for the generation of these hydrocarbons from marine kerogen (Ea = 50‐74kcal, A = 1.0×10¹⁴ s^?1 for C_1‐5; and Ea = 48‐72kcal, A=3.9×10¹³ s^?1 for C₁, respectively). Using these kinetic parameters, both the yields and timings of C_1‐5 and C₁ hydrocarbons generated from Cambrian source rocks and from in‐reservoir cracking of oil in Ordovician strata were predicted for selected wells along a north‐south profile in the SW of the basin. Thermodynamic conditions for the cracking of oil and kerogen were modelled within the context of the geological framework. It is suggested that marine kerogen began to crack at temperatures of around 120°C (or 0.8 %Ro) and entered the gas window at 138°C (or 1.05 %Ro); whereas the marine oil began to crack at about 140 °C (or 1.1 %Ro) and entered the gas window at 158 °C (or 1.6%Ro). The main geological controls identified for gas accumulations in the Bachu Arch (Southwest Depression, SW Tarim Basin) include the remaining gas potential following Caledonian uplift; oil trapping and preservation in basal Ordovician strata; the extent of breaching of Ordovician reservoirs; and whether reservoir burial depths are sufficiently deep for oil cracking to have occurred. In the Maigaiti Slope and Southwest Depression, the timing of gas generation was later than that in the Bachu Arch, with much higher yields and generation rates, and hence better prospects for gas exploration. It appears from the gas generation kinetics that the primary source for the gases in the Hetianhe gasfield was the Southwest Depression.     

高含酸性气碳酸盐岩气藏流体敏感性实验研究

对川东北雷口坡组、嘉陵江组、飞仙关组、长兴组高含H，S及032的碳酸盐岩储层流体敏感性进行了实验研究，结果表明岩样速敏损害弱～强，水敏和盐敏损害中偏弱～极强，碱敏损害严重。岩石学分析揭示，川东北高含酸性气碳酸盐岩储层发育伊利石、微晶石英、白云石、方解石、硫化钙等潜在损害物质。钻井完井液侵入会破坏储层各物质间的原始动态平衡，诱发储层损害。主要损害机理为：①储层流体pH增加引起黏土矿物以及微晶石英失稳；②碱液与微晶石英、长石、白云石反应生成硅酸盐、高岭石、水镁石等新矿相；③流体矿化度改变可降低伊利石微粒间的连接力；④硫化钙水解产生OH^-，过量的OH-与Ca^2＋结合形成氢氧化钙沉淀；⑤储层含水饱和度和流体离子浓度改变，致使焦沥青脱附并在储层深部沉积；⑥硬石膏水化膨胀、分散运移。针对该气藏损害机理，可采用屏蔽暂堵技术以形成优质滤饼，有效降低储层流体敏感性损害。图5表2参10。     

徐深气田兴城开发区营一段火山岩气藏岩性岩相研究

徐深气田兴城开发区营城组一段火山岩气藏位于松辽盆地北部徐家围子断陷升平-兴城构造带上，储层以酸性火山岩为主，可分为火山熔岩和火山角砾岩两大类。岩相类型有爆发相、溢流相、火山沉积相、火山通道相和侵出相五种类型，其中爆发相和溢流相分布范围广、物性好。是有利的储集相带。根据地震反射参数，从内部反射结构和外部几何形态出发，结合反射同相轴的振幅和连续性，在地震反射剖面上识别出丘状、楔状、亚平行状、柱状和伞状五种地震相类型，这些地震相类型与对应井点处单井相解释结果一致，与岩相类型对应关系明确。在剖面相准确识别的基础上，编制火山岩相平面分布图，为优选建产区块和部署开发井位提供依据。     

不同压力下气层岩样m、n值变化的实验研究

胶结指数m和饱和度指数n变化规律的研究一直是岩石物理学家和测井解释分析家关注的问题。压力是影响m、n的重要因素,但迄今为止,仍未取得可使多数人接受的一般性结论。实验开展了低孔隙度低渗透率气层岩样在不同压力条件下的电阻率测量,在考虑孔隙度随压力变化的基础上建立了m、n参数随压力变化的关系,得出结论:某些地区的气层岩样在压力增大时即使考虑孔隙度变化,m值增大,n值减小。     

井下气液分离及回注技术研究现状分析

气井产水量的不断增加对天然气生产构成严重威胁，其影响越来越受到人们的关注和重视。使用井下气液分离及回注技术，可以降低举升和处理费用，增加生产寿命，提高采收率，减少环境污染，简化地面分离设备，提高投资效益。针对井下分离及回注技术研究现状进行了分析，给出了并下气液分离及回注形式、适用条件和技术设计、应用方面的结论。     

Autothermal two-stage gasification of low-density waste-derived fuels

In order to increase the efficiency of waste utilization in thermal conversion processes, pre-treatment is advantageous. With the Herhof Stabilat^® process, residual domestic waste is upgraded to waste-derived fuel by means of biological drying and mechanical separation of inerts and metals. The dried and homogenized waste-derived Stabilat^® fuel has a relatively high calorific value and contains high volatile matter which makes it suitable for gasification. As a result of extensive mechanical treatment, the Stabilat^® produced is of a fluffy appearance with a low density. A two-stage gasifier, based on a parallel-arranged bubbling fluidized bed and a fixed bed reactor, has been developed to convert Stabilat^® into hydrogen-rich product gas. This paper focuses on the design and construction of the configured laboratory-scale gasifier and experience with its operation. The processing of low-density fluffy waste-derived fuel using small-scale equipment demands special technical solutions for the core components as well as for the peripheral equipment. These are discussed here. The operating results of Stabilat^® gasification are also presented.