放空尾气回收技术在塔中油田的应用

塔中油田为解决油气生产过程中排放的放空尾气给油田节能环保工作带来的压力,采用移动撬装天然气处理装置回收放空尾气技术。大量放空尾气经脱硫、脱水、脱烃、增压后,再利用CNG罐车拉运至尾气回收站回收利用。尾气回收利用技术的实施节约了大量天然气,降低了油气田开发对环境的影响。     

输气管道放空天然气回收方案探讨

本文结合输气管理处输气管道放空模式及现状,根据管线放空的实际数据,提出了一套切实可行的输气管道放空天然气回收实施方案。     

天然气净化厂放空废气对环境的影响及控制措施

天然气净化厂除正常生产有工艺废气排放外,传统装置检修开停产过程、供电或设备异常情况下,会有大量酸气、原料气通过放空火炬燃烧后排放。文章主要分析了天然气净化装置放空废气排放情况及其对周边环境的影响,阐述了异常放空、检修开停产过程原料气和酸气放空的控制措施及其环境效益。     

天然气处理站节能减排措施研究与应用

新疆油田公司采油二厂81~#天然气处理站为解决天然气放空所造成的能源浪费及对大气环境的污染,对原工艺流程进行优化改造。文章介绍该处理站各套装置运行特点,分析了天然气放空的几种原因,并通过两个增压站停机检修期间流程改造、罐区天然气放空线改造、检修期间2套浅冷装置的流程优化等针对性措施,全年累计减少天然气放空3000×10~4Nm~3左右,增加经济效益约3000万元,同时减少H_2S排放约524 kg。     

气田放空天然气减排技术探讨

随着低碳发展理念的不断深入,放空天然气带来的资源浪费与温室气体排放问题日益成为气田节能减排的关注重点之一。文章结合气田放空天然气排放特点,着重探讨国内外回收利用现状,在分析西南油气田减排技术需求的基础上提出适宜的减排技术建议,包括：开发井口放空气撬装式回收装置,开展增压机放空天然气减排技术研究,开展火炬气减排技术研究。通过对此类技术群的继续开发与应用,为气田下一步减排行动提供技术参考。     

低压放空天然气的高效再利用

为了提高试采放空天然气的利用率,考虑将不能输送的放空低压气进行技术增压,达到输送压力后,使其进入油气处理装置进行分离,其中一部分通过注气压缩机回注至地层,保持地层压力,提高油田凝析油采收率和延长油气田开发时间,实现低压气的高效利用。对站外试采井的低压放空气进行增压回收,减少了天然气资源浪费,实现了向资源节约型、环境保护企业的健康发展。     

排气放空消声器

由武汉市宏森环保技术工程有限责任公司开发的排气放空消声器，适用于钢铁、冶金、电力、石化、锅炉等行业各种气体（空气、氧气、氮气、蒸汽等）排气放空噪声的降低。     

小孔喷注消声器在蒸汽放空过程中的应用

本主要介绍了小孔喷注消声器在余热发电热发电蒸汽放空过程中的应用,降噪效果显,收到了良好的环境效益和社会效益。     

低压天然气回收再利用与节能环保

凝析油气藏在开采后期,由于地层压力自然递减加快,开采难度加大,而后期的工业及民用天然气需求量不断增加,导致凝析气藏产气量逐年缩减与天然用量逐步增多的矛盾日益明显。为缓解这一矛盾,考虑将不能输送的放空低压气进行技术增压,达到输送压力后,进入输送管道,从而增加天然气输送量,减少天然气放空对环境的污染。     

炼油厂火炬气的回收利用

通过在炼油厂放空系统上加装三组调节阀，将加热炉燃油喷嘴改为燃气喷嘴，使以前废弃烧掉的火炬气克分回收利用，即保护了环境，节约了能源，又提高了经济效益。     

站场伴生气减排回收工艺研究与应用

针对部分油田站场因伴生气量低造成的燃烧排放或无效放空的生产现状,研制了一种基于双U型管气液分离、气体过滤、阀前调压稳压和止回阀的组合式回收装置。对组合式回收装置进行了功能测试,并在17座站场现场应用,供气系统压力平稳,加热炉正常运行,实现了低气油比站场伴生气100%回收利用,有利于油田安全环保、节能减排与清洁生产。     

建立高含硫气田生态监测体系分析

针对西南某气田投产运行后,净化厂尾气、集气站火炬等正常生产和事故性放空等会排放大量二氧化硫的问题,及其对周边生态环境产生影响的现实,研究建立气田生态环境监测体系。通过现场踏勘、资料收集等手段,提出建立气田生态监测的布点网络、生态监测方法体系,重点探讨生物多样性及典型植物监测方法。通过在该气田实际监测得出该生态监测体系具有科学性、完整性、有效性等特点。     

芳烃石油树脂生产的环境保护

乙烯装置的副产品在综合利用中存在着严重的环境污染问题。中原油田采取了一些措施。用催化剂对生产尾气进行吸收,将有毒的氟化物转化为钙盐用于磷肥生产;将石油树脂聚合液中BF3脱除,防止对大气、水进行污染;用冷却回收工艺对减压蒸馏放空的芳烃气体进行处理。通过上述治理大大改善了企业的环境,有效地防止了环境污染。     

Capturing fugitive methane emissions from natural gas compressor buildings

Fugitive methane emissions account for about 50% of the greenhouse gas (GHG) emissions from the Canadian conventional oil and gas sector. Sources include leaks in natural gas transmission facilities such as pipelines and compressor stations. There are three sources of methane emissions in a compressor station. The first is emissions resulting from incomplete combustion in the engine; the second is leaks in valves, flanges and other equipment in the building; and the third results from instrument venting. Fugitive methane emissions may be in low concentration relative to air, and thus cannot be destroyed by conventional combustion (below flammability limits of about 5-16%). The present study investigates the feasibility of capturing methane emissions from a compressor station. Computer modelling of the flow patterns of lean methane emissions inside the building is used to show the influence of doors, vents and leak location. Simulations show that for a typical building most fugitive methane exits through the ridge vent provided that the main doors remain closed. When the extraction rate through the ridge vent is controlled, the methane concentration is at acceptable levels for destruction in a catalytic flow reverse reactor, that is, in the range of 0.1-1% by volume.     

Natural analogue of the rise and dissolution of liquid CO2 in the ocean

The behavior of natural carbon dioxide (CO₂) droplets (8–10 mm in diameter) were observed in a seafloor hydrothermal system at the Okinawa Trough. The natural CO₂ droplet contain 95–98% of CO₂, 2–3% of H₂S, and other gas species. The ascending CO₂ droplets were tracked by a remotely operated vehicle (ROV), and depth, temperature, salinity, pH and partial pressure of CO₂ (pCO₂) in seawater near the CO₂ droplets were measured during droplet ascent by a conductivity-temperature-depth sensor (CTD) and in situ pH/pCO₂ sensor. The visual images of the rising CO₂ droplets were recorded with a high definition television camera on the ROV. A mapping survey (400 m × 400 m; 4 horizontal layers) revealed a dominant distribution of low pH area over the natural CO₂ venting site. The size and rise rate of CO₂ droplets decreased during their ascent in the water column from depths of 1424 to 679 m (a tracking interval of 745 m). The CO₂ droplets dissolved gradually to become small flakes of CO₂ hydrate while rising, and these ascending flakes were found to disappear at 679 m depth. Although a pH as low as 5 was detected just above the liquid CO₂ venting site on the seafloor, no detectable pH depression in the water column ambient to the rising CO₂ droplets was observed. The results of the pH mapping survey showed only localized pH depression over the CO₂ venting site.