RU2003102599A - METHOD FOR USE OF REMOVED HEAT IN THE PROCESS OF RESTORING CARBON DIOXIDE - Google Patents

METHOD FOR USE OF REMOVED HEAT IN THE PROCESS OF RESTORING CARBON DIOXIDE

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Publication number
RU2003102599A
RU2003102599A RU2003102599/15A RU2003102599A RU2003102599A RU 2003102599 A RU2003102599 A RU 2003102599A RU 2003102599/15 A RU2003102599/15 A RU 2003102599/15A RU 2003102599 A RU2003102599 A RU 2003102599A RU 2003102599 A RU2003102599 A RU 2003102599A
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RU
Russia
Prior art keywords
carbon dioxide
tower
regeneration tower
absorbing liquid
liquid
Prior art date
Application number
RU2003102599/15A
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Russian (ru)
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RU2237172C1 (en
Inventor
Масаки ИИДЗИМА
Original Assignee
Мицубиси Хэви Индастриз, Лтд.
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Priority claimed from JP2002024528A external-priority patent/JP3814206B2/en
Application filed by Мицубиси Хэви Индастриз, Лтд. filed Critical Мицубиси Хэви Индастриз, Лтд.
Publication of RU2003102599A publication Critical patent/RU2003102599A/en
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Publication of RU2237172C1 publication Critical patent/RU2237172C1/en

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Claims (4)

1. Способ использования отводимой теплоты в процессе восстановления диоксида углерода, который включает в себя следующие операции: использование блока (20) восстановления диоксида углерода, который содержит градирню (21), абсорбционную башню (22) для абсорбции диоксида углерода при помощи абсорбирующей жидкости и регенерационную башню (23) для регенерации абсорбирующей жидкости, подача отходящих газообразных продуктов сгорания в градирню (21) для охлаждения отходящих газообразных продуктов сгорания, подача охлажденных отходящих газообразных продуктов сгорания в абсорбционную башню (22) таким образом, чтобы они входили в контакт с регенерированной абсорбирующей жидкостью, поступающей из регенерационной башни (23) для абсорбции диоксида углерода из отходящих газообразных продуктов сгорания с регенерированной абсорбирующей жидкостью, в результате чего на дне указанной абсорбционной башни (22) накапливается абсорбирующая жидкость с абсорбированным диоксидом углерода, нагревание абсорбирующей жидкости с абсорбированным диоксидом углерода за счет теплообмена (35) с регенерированной абсорбирующей жидкостью, поступающей из регенерационной башни (23), подача нагретой абсорбирующей жидкости с абсорбированным диоксидом углерода в регенерационную башню (23), нагревание дна регенерационной башни (23) с использованием насыщенного пара для разделения абсорбирующей жидкости с абсорбированным диоксидом углерода на диоксид углерода и регенерированную абсорбирующую жидкость и выпуск и рекуперация отделенного диоксида углерода из регенерационной башни (23), в котором возвратная горячая вода нагревается за счет по меньшей мере одного теплообмена, выбранного из группы, в которую входят теплообмен (37) с регенерированной абсорбирующей жидкостью после теплообмена, теплообмен (40) с диоксидом углерода, удаляемым из регенерационной башни (23), и теплообмен (44) с насыщенной водой после нагревания дна регенерационной башни (23), в результате чего получают горячую воду.1. The method of using the heat removed in the process of carbon dioxide recovery, which includes the following operations: using a carbon dioxide recovery unit (20) that contains a cooling tower (21), an absorption tower (22) for absorbing carbon dioxide using an absorbing liquid, and regeneration tower (23) for the regeneration of the absorbing liquid, the supply of exhaust gaseous products of combustion in the tower (21) for cooling the exhaust gaseous products of combustion, the supply of cooled exhaust gaseous x of the combustion products into the absorption tower (22) so that they come into contact with the regenerated absorbent liquid coming from the regeneration tower (23) to absorb carbon dioxide from the exhaust gaseous products of combustion with the regenerated absorbing liquid, resulting in the bottom of the specified absorption towers (22) accumulates an absorbing liquid with absorbed carbon dioxide, heating the absorbing liquid with absorbed carbon dioxide due to heat transfer (35) from the regenerators with an absorbent liquid coming from the regeneration tower (23), supplying a heated absorbent liquid with absorbed carbon dioxide to the regeneration tower (23), heating the bottom of the regeneration tower (23) using saturated steam to separate the absorbing liquid with absorbed carbon dioxide into carbon dioxide, and regenerated absorbent liquid and the release and recovery of the separated carbon dioxide from the regeneration tower (23), in which the return hot water is heated by at least One heat transfer selected from the group consisting of heat transfer (37) with regenerated absorbing liquid after heat transfer, heat transfer (40) with carbon dioxide removed from the regeneration tower (23), and heat transfer (44) with saturated water after heating the bottom of the regeneration towers (23), resulting in hot water. 2. Способ по п.1, отличающийся тем, что отходящие газообразные продукты сгорания представляют собой отходящие газы из котла (1) или газовой турбины электростанции.2. The method according to claim 1, characterized in that the exhaust gaseous products of combustion are exhaust gases from the boiler (1) or the gas turbine of the power plant. 3. Способ по п.1, отличающийся тем, что абсорбирующей жидкостью является жидкий амин.3. The method according to claim 1, characterized in that the absorbing liquid is a liquid amine. 4. Способ по п.1, отличающийся тем, что возвратную горячую воду нагревают сначала при помощи теплообмена (37) с регенерированной абсорбирующей жидкостью после теплообмена, затем при помощи теплообмена (40) с диоксидом углерода, удаляемым из регенерационной башни (23), и, наконец, при помощи теплообмена (44) с насыщенной водой после нагревания дна регенерационной башни (23), в результате чего получают горячую воду.4. The method according to claim 1, characterized in that the return hot water is heated first by heat exchange (37) with the regenerated absorbent liquid after heat exchange, then by heat exchange (40) with carbon dioxide removed from the regeneration tower (23), and finally, by heat exchange (44) with saturated water after heating the bottom of the regeneration tower (23), resulting in hot water.
RU2003102599/15A 2002-01-31 2003-01-30 Method of utilization of heat abstracted in process of reduction of carbon dioxide RU2237172C1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2002-24528 2002-01-31
JP2002024528A JP3814206B2 (en) 2002-01-31 2002-01-31 Waste heat utilization method of carbon dioxide recovery process

Publications (2)

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RU2003102599A true RU2003102599A (en) 2004-07-27
RU2237172C1 RU2237172C1 (en) 2004-09-27

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US (1) US6764530B2 (en)
EP (1) EP1336724B1 (en)
JP (1) JP3814206B2 (en)
CA (1) CA2414615C (en)
DE (1) DE60200756T2 (en)
DK (1) DK1336724T3 (en)
NO (1) NO334438B1 (en)
RU (1) RU2237172C1 (en)

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