首页> 外国专利> METHOD OF LIQUEFACTION OF THE STREAM OF THE NATURAL GAS RICH WITH THE HYDROCARBONS WITH THE SIMULTANEOUS EXTRACTION OF C3+ RICH FRACTION WITH THE HIGH YIELD

METHOD OF LIQUEFACTION OF THE STREAM OF THE NATURAL GAS RICH WITH THE HYDROCARBONS WITH THE SIMULTANEOUS EXTRACTION OF C3+ RICH FRACTION WITH THE HIGH YIELD

机译:高产C 3 + 富馏分同时萃取富集天然气的天然气液化方法

摘要

FIELD: natural gas industry; other industries; methods of liquefaction of the rich with the hydrocarbons gaseous stream with the simultaneous extraction of С3+-rich fraction.;SUBSTANCE: the invention presents the method of liquefaction of the rich with the hydrocarbons stream, first of all the stream of the natural gas with the simultaneous extraction of С3+ - rich fraction with the high yield at the expense of the heat-exchange of the rich with the hydrocarbons stream at least with three having the different composition mixed cooling agents of the cascade correspondingly consisting of at least three refrigeration cycles. According to the invention the rich with the hydrocarbons stream (1, 1') is exposed to dilation (X) before its division into C2-- the rich fraction and С3+ - the rich fraction. The exposed to dilation the rich with the hydrocarbons stream (2)is fed to the stage of absorption (Т1) of the hydrocarbons C3+ , dividing it at this stage into the fed for liquefaction (Е2, ЕЗ) С2- - rich fraction (3) and into the first condensate fraction (8). The fed for liquefaction C2-- rich fraction (3) is compressed (V) before its liquefaction (Е2, ЕЗ). The first condensate fraction (8) in the heated up (E) state is fed to the stage of the topping (Т2) of the hydrocarbons С2. In the capacity of the vat residue formed at the stage of the topping (Т2) of the hydrocarbons С2, they receive with the high yield the second fraction, С3+ - the rich condensate fraction (11). In the capacity of the head faction formed at the stage of the topping (Т2) of hydrocarbons С2, take out C3- - rich gaseous fraction, which is partially condensed (E), and the received condensate is fed (10) into the stage of absorption (Т1) of the hydrocarbons С3 as the absorbing agent. Usage of the invention will allow to ensure along with the liquefaction of the stream of the natural gas simultaneously to receive together with the rich yield of hydrocarbons С3+ - rich fraction.;EFFECT: the invention ensures along with the liquefaction of the stream of the natural gas simultaneous production of the rich yield of hydrocarbons С3+ - rich fraction.;9 cl, 2 dwg
机译:领域:天然气工业;其他行业;方法:同时萃取富含С 3 + 馏分的富集烃气态液化方法。物质:本发明提出了一种富集烃气态液化液的方法,首先是所有天然气流同时以高收率同时提取С 3 + -富馏分,但要消耗富烃与烃流的热交换,至少三个要级联的不同组成的混合冷却剂相应地包括至少三个制冷循环。根据本发明,具有烃料流(1,1')的浓烃在其分成C 2- -浓馏分和С之前暴露于膨胀(X)。 3 + -丰富分数。处于膨胀状态的富含烃物流(2)的烃被送入烃C 3 + 的吸收阶段(Т1),在此阶段将其分为液化进料(Е2, ЕЗ)С 2- -富馏分(3)进入第一个冷凝液馏分(8)。富液化的进料C 2- -的馏分(3)在液化(Е2,ЕЗ)之前被压缩(V)。将处于加热(E)状态的第一冷凝馏分(8)送入烃С 2 的顶部浇注(Т2)阶段。 在碳氢化合物С 2 的顶部(Т2)阶段形成的大桶残留物中,它们以高收率获得第二部分С 3+ -富冷凝水馏分(11)。在碳氢化合物С 2 打顶阶段形成的主要派系的能力中,取出富含C 3-的气态馏分,将其部分冷凝。 (E),然后将接收到的冷凝水供入(10)到作为吸收剂的烃С 3 的吸收阶段(Т1)。本发明的使用将允许确保与天然气流的液化一起同时接收到富含碳氢化合物的富集的С 3 + -馏分。液化天然气流同时生产富烃的富油С 3 + -富馏分。; 9 cl,2 dwg

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