公开(公告)号：US20110092355A1

公开(公告)日：2011-04-21

申请号：US12752405

申请日：2010-04-01

Applicant: Masaki IIJIMA ,  Masahiko TATSUMI ,  Yasuyuki YAGI ,  Kouki OGURA

Inventor： Masaki IIJIMA ,  Masahiko TATSUMI ,  Yasuyuki YAGI ,  Kouki OGURA

IPC: B01J20/34 ,  B01D53/96 ,  B01D11/02

CPC classification number: B01D53/1425 ,  B01D19/0005 ,  B01D53/1412 ,  B01D53/1462 ,  Y02C10/06 ,  Y02C10/08 ,  Y10S502/517 ,  Y10S502/518

Abstract: A reclaiming apparatus 106 includes: a sealed container 106a that is an absorbent reservoir for storing therein a part of an absorbent that has absorbed CO2 in flue gas, and a heater that heats the absorbent stored in the sealed container 106a. The reclaiming apparatus 106 distributes a part of the absorbent stored in the sealed container 106a, and brings the distributed absorbent into counter-current contact with steam. Because a part of the absorbent stored in the absorbent reservoir is brought into counter-current contact with the steam, absorbent component contained therein becomes volatilized, and is separated from depleted materials. In this manner, the absorbent component can be extracted from the depleted materials, and a loss of the absorbent can be reduced.

Abstract translation: 回收装置106包括：密封容器106a，其是用于在其中存储已经吸收烟道气中的CO 2的吸收剂的吸收容器，以及加热器，其加热存储在密封容器106a中的吸收剂。 回收装置106分配存储在密封容器106a中的一部分吸收剂，并使分散的吸收剂与蒸汽逆流接触。 因为储存在吸收剂储存器中的吸收剂的一部分与蒸汽逆流接触，所以包含在其中的吸收组分变得挥发，并与耗尽的材料分离。 以这种方式，可以从耗尽的材料中提取吸收组分，并且可以减少吸收剂的损失。

公开(公告)号：US20090193970A1

公开(公告)日：2009-08-06

申请号：US12200277

申请日：2008-08-28

Applicant: Masaki IIJIMA

Inventor： Masaki IIJIMA

IPC: B01D53/62 ,  B01D53/78

CPC classification number: B01D53/1406 ,  B01D53/1425 ,  B01D61/14 ,  B01D61/147 ,  B01D65/02 ,  B01D2257/504 ,  B01D2311/04 ,  B01D2321/08 ,  B01D2321/185 ,  Y02C10/04 ,  Y02C10/06 ,  B01D2311/2626

Abstract: A CO2 recovery system includes an absorption tower that removes CO2 from exhaust gas, a regeneration tower that regenerates a rich solution, and a separation drum that condensates steam in CO2 gas released from the regeneration tower and separates water. The CO2 recovery system further includes a filtration membrane apparatus that filters solid content remaining in the lean solution using a filter, and cleans the filter using condensed water as cleaning water and again return the condensed water into the system. The CO2-absorbing solution attached to the filter is collected and the filter is cleaned without diluting the CO2-absorbing solution upon replacement of the filter.

Abstract translation: 二氧化碳回收系统包括从废气中除去二氧化碳的吸收塔，再生富含溶液的再生塔，以及将从再生塔排出的二氧化碳气体中的蒸汽冷凝并分离水的分离鼓。 二氧化碳回收系统还包括过滤膜装置，其使用过滤器对残留在稀溶液中的固体含量进行过滤，并使用冷凝水作为清洗水清洗过滤器，并再次将冷凝的水返回到系统中。 收集附着在过滤器上的二氧化碳吸收溶液，在更换过滤器时，不用稀释二氧化碳吸收溶液清洗过滤器。

公开(公告)号：US20130014430A1

公开(公告)日：2013-01-17

申请号：US13547272

申请日：2012-07-12

Applicant: Masaki IIJIMA

Inventor： Masaki IIJIMA

IPC: B01J8/00 ,  F01K13/00 ,  F01D15/10 ,  C10L1/04

CPC classification number: C10G3/42 ,  B01J8/02 ,  B01J8/0285 ,  B01J2208/00168 ,  C10G3/49 ,  C10G2300/805 ,  C10G2400/02 ,  C10L1/06 ,  C10L2270/023 ,  C10L2290/06 ,  F01K13/00 ,  Y02P30/20

Abstract: A method for generating electric power and for producing gasoline from methanol, includes the steps of: synthesizing gasoline by reacting methanol under a catalyst; recovering heat generated from the gasoline synthetic reaction of methanol by cooling the reaction with coolant to vaporize the coolant; and generating electric power by using the coolant vapor produced in the heat recovery. The power generation step may include generating electric power with a plurality of steam turbines in series, e.g., a high-pressure turbine, a medium-pressure turbine, and a low-pressure turbine.

Abstract translation: 一种从甲醇产生电力和生产汽油的方法，包括以下步骤：通过在催化剂下使甲醇反应合成汽油; 通过冷却与冷却剂的反应来蒸发冷却剂来回收由汽油合成甲醇反应产生的热量; 并通过使用在热回收中产生的冷却剂蒸汽发电。 发电步骤可以包括利用多个串联的蒸汽轮机（例如高压涡轮机，中压涡轮机和低压涡轮机）来产生电力。

公开(公告)号：US20120255305A1

公开(公告)日：2012-10-11

申请号：US13338408

申请日：2011-12-28

Applicant: Masaki IIJIMA

Inventor： Masaki IIJIMA

IPC: F01K13/00

CPC classification number: B01D53/1425 ,  B01D53/1475 ,  B01D53/62 ,  B01D2257/504 ,  B01D2258/0283 ,  B01D2259/65 ,  F01K7/06 ,  F01K19/00 ,  F23J15/006 ,  F23J2215/50 ,  F23J2219/40 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02E20/326

Abstract: A carbon dioxide recovery system includes a high-pressure 11, a boiler 15, a carbon dioxide recovery unit 24 that includes a carbon dioxide absorber 21 that absorbs and reduces carbon dioxide in flue gas G emitted from the boiler 15 using a carbon dioxide absorbent and an absorbent regenerator 23 that regenerates a carbon dioxide absorbent having absorbed the carbon dioxide using a regenerating superheater 22 to obtain a regenerated carbon dioxide absorbent, a high-temperature and high-pressure steam extraction line L11 that extracts the high-temperature and high-pressure steam 14 from the boiler 15 before the steam is introduced into the high-pressure turbine 11, an auxiliary turbine 32 that recovers power with the high-temperature and high-pressure steam 14, and a steam supply line L12 that supplies emission steam 33 emitted from the auxiliary turbine 32 to the regenerating superheater 22 to be used as a heat source.

Abstract translation: 二氧化碳回收系统包括高压11，锅炉15，二氧化碳回收单元24，二氧化碳回收单元24包括二氧化碳吸收器21，二氧化碳吸收器21使用二氧化碳吸收剂吸收和还原从锅炉15排出的烟道气G中的二氧化碳， 吸收剂再生器23，其使用再生过热器22再生吸收了二氧化碳的二氧化碳吸收剂，以获得再生二氧化碳吸收剂;高温高压蒸汽提取管线L11，其提取高温高压 在将蒸汽引入高压涡轮机11之前，来自锅炉15的蒸汽14，用高温高压蒸汽14回收动力的辅助涡轮机32和排出的排出蒸气33的蒸汽供给管路L12 从辅助涡轮32到再生过热器22，用作热源。

公开(公告)号：US20090252659A1

公开(公告)日：2009-10-08

申请号：US12098639

申请日：2008-04-07

Applicant: Masaki IIJIMA ,  Hasham MUKADAM ,  Ronald M. WEINER

Inventor： Masaki IIJIMA ,  Hasham MUKADAM ,  Ronald M. WEINER

IPC: F01N3/00

CPC classification number: F01N5/02 ,  F01K23/10 ,  F22B1/1815 ,  F22B1/1861 ,  F23J2215/50 ,  Y02E20/326 ,  Y02P20/13 ,  Y02T10/16

Abstract: A method for flue gas treatment includes causing a combustion in a boiler using at least a part of a flue gas emitted from a gas turbine and introduced from at least one of an upstream side and a downstream side of an exhaust heat recovery boiler, which recovers a high-temperature heat of the flue gas, so as to increase a concentration of carbon dioxide in the flue gas, and recovering carbon dioxide in a carbon dioxide recovery apparatus.

Abstract translation: 一种用于烟气处理的方法，包括使用至少一部分从燃气轮机排出的废气排放并从废热回收锅炉的上游侧和下游侧引入的锅炉中的燃烧， 烟气的高温热，从而增加烟道气中二氧化碳的浓度，并回收二氧化碳回收装置中的二氧化碳。

公开(公告)号：US20100319532A1

公开(公告)日：2010-12-23

申请号：US12645591

申请日：2009-12-23

Applicant: Masaki IIJIMA ,  Kouki OGURA ,  Masahiko TATSUMI ,  Yasuyuki YAGI

Inventor： Masaki IIJIMA ,  Kouki OGURA ,  Masahiko TATSUMI ,  Yasuyuki YAGI

IPC: B01D53/96 ,  B01D53/18 ,  B01D53/62 ,  B01D53/78

CPC classification number: B01D53/62 ,  B01D53/1412 ,  B01D53/1425 ,  B01D53/1475 ,  B01D53/77 ,  B01D2251/80 ,  B01D2257/504 ,  Y02A50/2342 ,  Y02C10/06

Abstract: Provided are a CO2 absorber that reduces CO2 contained in flue gas; a regenerator that reduces CO2 contained in rich solvent absorbing CO2 to regenerate the rich solvent, so that lean solvent having the CO2 reduced in the regenerator is reused in the CO2 absorber; a heat exchanger that allows the rich solvent to exchange heat with the lean solvent; and a controller that controls to extract rich solvent portion that is part of the rich solvent, to allow the rich solvent portion to by pass the heat exchanger, and to be supplied into the top of the regenerator without exchanging heat so as to minimize a sum of an enthalpy that is taken out of the regenerator as CO2 gas accompanying steam and an enthalpy of the lean solvent after heat exchange with the rich solvent in the heat exchanger.

Abstract translation: 提供一种减少烟道气中二氧化碳的二氧化碳吸收器; 一种再生器，其减少富溶剂中含有的二氧化碳中的二氧化碳以再生富溶剂，使得在再生器中减少的二氧化碳的贫溶剂在CO 2吸收器中重复使用; 允许富溶剂与贫溶剂进行热交换的热交换器; 以及控制器，其控制提取作为富溶剂的一部分的富溶剂部分，以允许富溶剂部分通过热交换器，并且供给到再生器的顶部而不交换热量，以使总和最小化 的焓，其作为伴随蒸汽的CO 2气体和在热交换器中与富溶剂热交换后的贫溶剂的焓而从再生器中取出。

公开(公告)号：US20100224064A1

公开(公告)日：2010-09-09

申请号：US12581649

申请日：2009-10-19

Applicant: Masaki IIJIMA

Inventor： Masaki IIJIMA

IPC: B01D45/00

CPC classification number: F23L17/005 ,  B01D53/346 ,  B01D53/62 ,  B01D2257/504 ,  F23J15/006 ,  F23J2215/50 ,  F23J2217/20 ,  F23L11/00 ,  F23L13/06 ,  Y02C10/04 ,  Y02E20/326 ,  Y10T137/4643 ,  Y10T137/86212

Abstract: An air pollution control apparatus according to an embodiment of the present invention includes: a stack that discharges flue gas discharged from a boiler outside; a blower that is provided downstream of the stack and draws in the flue gas; and a CO2 recovering apparatus that recovers CO2 in the flue gas drawn in by the blower. The stack includes a controlling unit that suppresses release of the flue gas outside from the stack and suppresses inflow of atmosphere to the stack, and the controlling unit is a channel forming unit that forms a serpentine channel through which the flue gas and the atmosphere in the stack flow.

Abstract translation: 根据本发明实施例的空气污染控制装置包括：排出从锅炉外部排出的烟道气的堆; 提供在烟囱下游并吸入烟道气的鼓风机; 以及CO 2回收装置，其回收由鼓风机吸入的烟道气中的CO 2。 该堆叠包括控制单元，该控制单元抑制烟道气从堆叠中的释放，并抑制气氛向堆叠的流入，并且控制单元是形成蛇形通道的通道形成单元，通过该通道形成单元，烟道气体和 堆流。

公开(公告)号：US20080203036A1

公开(公告)日：2008-08-28

申请号：US12022468

申请日：2008-01-30

Applicant: Masaki IIJIMA ,  Takashi KAMIJO

Inventor： Masaki IIJIMA ,  Takashi KAMIJO

IPC: B01D29/62

CPC classification number: B01D53/73 ,  B01D53/1425 ,  B01D53/1475 ,  B01D53/62 ,  Y02C10/04 ,  Y02C10/06 ,  Y02P20/152

Abstract: A solution contained in a regeneration tower is supplied to a filtering unit. The filter unit filters out solid particles contained in the solution. A washing unit washes out with backwash water solid particles filtered out by the filter unit. An evaporating unit receives the backwash water containing the solid particles, and heats received backwash water thereby obtaining solid-particles concentrated backwash water.

Abstract translation: 包含在再生塔中的溶液被提供给过滤单元。 过滤器单元过滤掉溶液中包含的固体颗粒。 用洗涤水清洗洗涤单元，过滤单元过滤出的反冲洗水固体颗粒。 蒸发单元接收含有固体颗粒的回洗水，并加热接收反冲洗水，从而获得固体颗粒集中的反冲洗水。