首页> 外文会议>University of Oklahoma Education Engineering Geosciences >LNG PRE-TREATMENT-LOWER LIFE CYCLE COSTS WITH UOP SEPARSIV ADSORBENT PROCESS FOR HEAVY HYDROCARBON REMOVAL FROM LEAN NATURAL GAS
【24h】

LNG PRE-TREATMENT-LOWER LIFE CYCLE COSTS WITH UOP SEPARSIV ADSORBENT PROCESS FOR HEAVY HYDROCARBON REMOVAL FROM LEAN NATURAL GAS

机译:LNG预处理 - 利用UOP SELASIV吸附剂的寿命循环成本降低,用于从贫苯天然气中移除碳氢化合物

获取原文

摘要

Lean natural gas feeds are becoming common for newer North American LNG plants as many of these facilities process feed from unconventional sources. These new gas resources have more methane and less NGL's than conventional feeds. However, many lean feed gas sources contain disproportionately high amounts of heavy hydrocarbons (HHCs), which can be similar in magnitude to those found in the conventional feed gas. The amount of these heavy components can exceed the maximum amount allowed to avoid freezing in the liquefaction process. Components such as octane, nonane, benzene, and ethyl benzene are particularly challenging as even small amounts of these components can freeze at LNG temperatures. To prevent freezing of the heavies in LNG production, one of the requirements in the pretreatment step is the removal of heavy hydrocarbons (C6+). Traditionally, this is done using a distillation approach by a scrub column. It is difficult for a traditional distillation column to operate stably and efficiently on lean feed gas because there are not enough NGL components present to provide sufficient reflux and downward liquid traffic in the column. Possible solutions for providing the needed cold liquid include providing it from the downstream cold box or/and feed gas expansion. However, both options are very energy inefficient. If not properly handled, freezing of HHCs can become so severe that it is necessary to shut down and defrost the plant, leading to loss of LNG production and lost revenue. UOP has developed an alternative process for heavy hydrocarbon removal from lean natural gas, called SeparSIV. This adsorption-based process is built on commercially proven technology for water and heavy hydrocarbon removal to meet pipeline gas specifications. To further meet the more stringent specification for LNG, UOP's SeparSIV adsorption system uses a mix of adsorbents capable of removing C5+ to less than 0.1 mol% and BTEX to less than 1 ppmv from lean gas. This system operates at high pressure with a low pressure drop and does not require the gas expansion and recompression commonly found in an NGL extraction unit. The adsorption system is also very selective for heavy hydrocarbons without removing lighter ones. Also, UOP's SeparSIV can be designed to remove HHCs and water simultaneously in a single process unit. Other benefits of this new process will be discussed in later sections of this paper.
机译:对于新的北美LNG植物来说,瘦天然气饲料是常见的,因为许多这些设施从非传统来源饲料饲料。这些新的气体资源具有更多的甲烷和较少的NGL比常规饲料更少。然而,许多瘦进料气体源含有不成比例的大量重质烃(HHC),其可以与在常规进料气体中发现的那些相似。这些重组分的量可以超过允许在液化过程中避免冻结的最大量。辛烷,壬烷,苯和乙烯等组分特别具有挑战性,因为即使少量这些组分可以在LNG温度下冻结。为了防止液化天液生产中的悬浮液,预处理步骤中的要求之一是除去重质烃(C6 +)。传统上,这是使用汽油柱的蒸馏方法完成的。一种传统的蒸馏塔难以稳定,有效地在贫料气体上操作,因为没有足够的NGL组分在柱中提供足够的回流和向下液体交通。提供所需冷液体的可能溶液包括从下游冷箱或/和进料气体膨胀提供。但是,这两个选项都是非常能量低效的。如果没有正确处理,HHC的冻结可能会变得如此严重,有必要关闭和解冻植物,导致液化天然气生产和收入损失。 UOP开发了一种替代方法,用于从贫酸中去除贫烃,称为分离液。基于吸附的过程基于商业证明技术,用于达到管道气体规格的水和重质碳氢化合物。为了进一步满足LNG的更严格的规范,UOP的Sextsiv吸附系统使用能够从贫气体中除去C5 +至小于0.1mol%的吸附剂的混合物,从贫气体中少于1ppmV。该系统以低压下降的高压工作,不需要在NGL提取单元中常见的气体膨胀和再现。吸附系统对于重型烃也非常有选择,而不会去除较轻的碳氢化合物。此外,UOP的SELICSIV可以设计成在单个过程单元中同时去除HHC和水。在本文的稍后的部分中将讨论这一新进程的其他优势。

著录项

相似文献

  • 外文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号