公开(公告)号：US20160187060A1

公开(公告)日：2016-06-30

申请号：US14944854

申请日：2015-11-18

Applicant: Lars Kirchner

Inventor： Lars Kirchner

IPC: F25J3/04 ,  F25J3/08 ,  C01B13/02

CPC classification number: F25J3/04412 ,  C01B13/0248 ,  F25J3/04187 ,  F25J3/04745 ,  F25J3/0486 ,  F25J3/08 ,  F25J2200/34 ,  F25J2210/40 ,  F25J2220/44 ,  F25J2220/52 ,  F25J2235/50

Abstract: A method and plant for discharging components that are less volatile than oxygen from an air separation plant that contains a main heat exchanger a side condenser and a two-column distillation column system for nitrogen-oxygen separation. The side condenser is constructed as a condenser-evaporator and is arranged in a vessel. A part of the feed air is cooled in the main heat exchanger and liquefied at least in part in the side condenser. A first oxygen fraction is withdrawn in the liquid state from the low-pressure column, introduced into the vessel of the side condenser and in part vaporized. A purge stream is taken off from the bottom of the vessel in the liquid state and discharged or withdrawn as end product. The vessel has a mass transfer section above the side condenser, which mass transfer section corresponds to more than one theoretical plate and fewer than 10 theoretical plates.

Abstract translation: 一种用于排出比来自空气分离设备挥发性低的组分的方法和设备，所述空气分离设备包含主要热交换器侧冷凝器和用于氮 - 氧分离的双塔蒸馏塔系统。 侧冷凝器构造为冷凝器 - 蒸发器并且布置在容器中。 进料空气的一部分在主热交换器中被冷却，至少部分地在侧冷凝器中液化。 将第一氧气馏分从液体状态从低压塔排出，引入侧冷凝器的容器中并部分蒸发。 清洗流从液体状态的容器底部取出，作为最终产品排出或抽出。 容器在侧冷凝器上方具有传质部分，该传质部分对应于多于一个理论塔板和少于10个理论塔板。

公开(公告)号：US10330383B2

公开(公告)日：2019-06-25

申请号：US14944854

申请日：2015-11-18

Applicant: Lars Kirchner

Inventor： Lars Kirchner

IPC: F25J3/04 ,  C01B13/02 ,  F25J3/08

Abstract: A method and plant for discharging components that are less volatile than oxygen from an air separation plant that contains a main heat exchanger a side condenser and a two-column distillation column system for nitrogen-oxygen separation. The side condenser is constructed as a condenser-evaporator and is arranged in a vessel. A part of the feed air is cooled in the main heat exchanger and liquefied at least in part in the side condenser. A first oxygen fraction is withdrawn in the liquid state from the low-pressure column, introduced into the vessel of the side condenser and in part vaporized. A purge stream is taken off from the bottom of the vessel in the liquid state and discharged or withdrawn as end product. The vessel has a mass transfer section above the side condenser, which mass transfer section corresponds to more than one theoretical plate and fewer than 10 theoretical plates.

公开(公告)号：US09797654B2

公开(公告)日：2017-10-24

申请号：US14899031

申请日：2014-07-10

Applicant: Lars Kirchner ,  Dimitri Goloubev

Inventor： Lars Kirchner ,  Dimitri Goloubev

IPC: F25J3/00 ,  F25J3/04 ,  F25J3/06

CPC classification number: F25J3/04836 ,  F25J3/04018 ,  F25J3/04024 ,  F25J3/0406 ,  F25J3/0409 ,  F25J3/04157 ,  F25J3/04169 ,  F25J3/04181 ,  F25J3/04206 ,  F25J3/04218 ,  F25J3/0426 ,  F25J3/04309 ,  F25J3/04351 ,  F25J3/04412 ,  F25J3/04418 ,  F25J3/04424 ,  F25J3/04496 ,  F25J3/04581 ,  F25J3/04618 ,  F25J3/04812 ,  F25J3/0483 ,  F25J3/0486 ,  F25J3/04878 ,  F25J3/04884 ,  F25J3/04957 ,  F25J3/0605 ,  F25J3/066 ,  F25J2200/06 ,  F25J2200/54 ,  F25J2205/32 ,  F25J2205/34 ,  F25J2205/62 ,  F25J2205/70 ,  F25J2210/50 ,  F25J2230/04 ,  F25J2230/24 ,  F25J2230/30 ,  F25J2230/42 ,  F25J2235/52 ,  F25J2240/70 ,  F25J2250/04 ,  F25J2250/40 ,  F25J2250/50

Abstract: A method and device to produce oxygen by the low-temperature separation of air at variable energy consumption. A distillation column system comprises a high-pressure column, a low-pressure column and a main condenser, a secondary condenser and a supplementary condenser. Gaseous nitrogen from the high-pressure column is liquefied in the main condenser in indirect heat exchange with an intermediate liquid from the low-pressure column. A first liquid oxygen stream from the bottom of the low-pressure column is evaporated in the secondary condenser in indirect heat exchange with feed air to obtain a gaseous oxygen product. The supplementary condenser serves as a bottom heating device for the low-pressure column and is heated by means of a first nitrogen stream from the distillation column system, which nitrogen stream was compressed previously in a cold compressor.

公开(公告)号：US20160123662A1

公开(公告)日：2016-05-05

申请号：US14899031

申请日：2014-07-10

Applicant: Lars Kirchner ,  Dimitri Goloubev

Inventor： Lars Kirchner ,  Dimitri Goloubev

IPC: F25J3/04 ,  F25J3/06

CPC classification number: F25J3/04836 ,  F25J3/04018 ,  F25J3/04024 ,  F25J3/0406 ,  F25J3/0409 ,  F25J3/04157 ,  F25J3/04169 ,  F25J3/04181 ,  F25J3/04206 ,  F25J3/04218 ,  F25J3/0426 ,  F25J3/04309 ,  F25J3/04351 ,  F25J3/04412 ,  F25J3/04418 ,  F25J3/04424 ,  F25J3/04496 ,  F25J3/04581 ,  F25J3/04618 ,  F25J3/04812 ,  F25J3/0483 ,  F25J3/0486 ,  F25J3/04878 ,  F25J3/04884 ,  F25J3/04957 ,  F25J3/0605 ,  F25J3/066 ,  F25J2200/06 ,  F25J2200/54 ,  F25J2205/32 ,  F25J2205/34 ,  F25J2205/62 ,  F25J2205/70 ,  F25J2210/50 ,  F25J2230/04 ,  F25J2230/24 ,  F25J2230/30 ,  F25J2230/42 ,  F25J2235/52 ,  F25J2240/70 ,  F25J2250/04 ,  F25J2250/40 ,  F25J2250/50

Abstract: A method and device to produce oxygen by the low-temperature separation of air at variable energy consumption. A distillation column system comprises a high-pressure column, a low-pressure column and a main condenser, a secondary condenser and a supplementary condenser. Gaseous nitrogen from the high-pressure column is liquefied in the main condenser in indirect heat exchange with an intermediate liquid from the low-pressure column. A first liquid oxygen stream from the bottom of the low-pressure column is evaporated in the secondary condenser in indirect heat exchange with feed air to obtain a gaseous oxygen product. The supplementary condenser serves as a bottom heating device for the low-pressure column and is heated by means of a first nitrogen stream from the distillation column system, which nitrogen stream was compressed previously in a cold compressor.

Abstract translation: 通过在不同能量消耗下的空气的低温分离来产生氧气的方法和装置。 蒸馏塔系统包括高压塔，低压塔和主冷凝器，二级冷凝器和辅助冷凝器。 来自高压塔的气态氮在主冷凝器中与来自低压塔的中间液体间接热交换液化。 来自低压塔底部的第一液氧流在二次冷凝器中与进料空气间接热交换而蒸发，得到气态氧产物。 辅助冷凝器用作低压塔的底部加热装置，并通过来自蒸馏塔系统的第一氮气流加热，氮气流先前在冷压缩机中压缩。