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PROFITABLY RECOVER REFINERY BY-PRODUCT NGLS, HYDROGEN AND ETHYLENE/PROPYLENE

机译:适当回收炼油厂副产物NGLS,氢和乙烯/丙烯

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Refineries have long been dealing with constantly changing market conditions. Currently,reduced domestic gasoline consumption, required ethanol blending, improved vehicle miles per gallonand more stringent fuel quality specifications have exacerbated the situation. Capturing opportunities toimprove margins will be crucial for survival and sustained profitability.Over decades of operation, refinery fuel gas systems have become the repository for purge gasesfrom Fluidized Catalytic Cracking, Delayed Coking, Catalytic Reforming, Hydrotreating,Hydrocracking and other process units. Figure 1 illustrates the various sources of hydrocarbon offgasand hydrogen purge streams in a typical refinery. Flare gas recovery systems also contribute to thebuild-up of non-methane components in refinery fuel gas. Hydrogen concentrations of 50 volume percent (and higher) are not unusual. Segregating fuel gas blending streams and extracting hydrogen, NGLsand ethylene/propylene provides a moderate capital cost route to improved profitability, triggered by the"perfect storm" conditions of low natural gas cost (to replace the heating value of extracted gases) andhigher values for recovered components. Hydrogen recovery and purification avoids costs of onsitehydrogen manufacture or import from area pipelines. Capital costs vary widely, dependent on refinerysize / complexity and scope of targeted component recoveries. While there is no "typical" recoveryproject, case study has shown such projects have attractive economics with payback from 1 to 3 years.Capital costs ranged from less than $5 million to approximately $100 million.Technology strategies for extraction and purification include cryogenic, pressure swingadsorption (PSA), semi-permeable membranes, compression and gas treating. BHTS has developedoptimized configurations utilizing a combination of technologies to meet a refiner's specific recoveryand purity targets.An initial screening study provides in-depth understanding of the current operation and identifiesopportunities for segregation, extraction, treating and purification of hydrogen, NGLs and olefinfractions of various streams connected to the fuel gas system. This is followed by a comprehensiveanalysis which includes capital & operating cost estimating, equipment layout / constructability analysis,piping changes and utility / offsites impacts.
机译:精炼厂长期以来一直在应对不断变化的市场状况。目前, 减少国内汽油消耗,需要乙醇混合,提高每加仑汽车行驶里程 更加严格的燃油质量规范加剧了这种情况。抓住机会 提高利润率对于生存和持续盈利至关重要。 经过数十年的运营,炼油厂的燃气系统已成为吹扫气体的储存库 从流化催化裂化,延迟焦化,催化重整,加氢处理, 加氢裂化等工艺单元。图1说明了各种碳氢化合物废气源 和典型的精炼厂中的氢气吹扫流。火炬气回收系统也有助于 炼厂燃料气中非甲烷成分的积累。氢气浓度为50体积/每 分(或更高)并不罕见。分离燃气混合流并提取氢气,NGL 乙烯/丙烯为提高利润率提供了适度的资本成本途径,这是由 天然气成本低的“完美风暴”条件(用以替代提取气体的热值),以及 回收成分的值更高。氢气回收和纯化避免了现场成本 制氢或从区域管道进口氢气。资本成本差异很大,取决于炼油厂 目标组分回收的规模/复杂性和范围。虽然没有“典型的”恢复 案例研究表明,此类项目具有极佳的经济效益,投资回收期为1至3年。 资本成本从不到500万美元到大约1亿美元不等。 提取和纯化的技术策略包括低温,变压 吸附(PSA),半透膜,压缩和气体处理。 BHTS已开发 利用多种技术进行优化配置以满足炼油厂的特定回收率 和纯度目标。 初步筛选研究可提供对当前操作的深入了解并确定 氢,NGL和烯烃的分离,萃取,处理和纯化的机会 连接到燃气系统的各种物流的一部分。接下来是全面的 分析,包括资本和运营成本估算,设备布局/可施工性分析, 管道变化和公用事业/异地影响。

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