公开(公告)号：US20100329957A1

公开(公告)日：2010-12-30

申请号：US12872370

申请日：2010-08-31

申请人： Hiromitsu Nagayasu ,  Yasutoshi Ueda ,  Ryokichi Hamaguchi ,  Susumu Okino ,  Morio Kagami

发明人： Hiromitsu Nagayasu ,  Yasutoshi Ueda ,  Ryokichi Hamaguchi ,  Susumu Okino ,  Morio Kagami

IPC分类号： B01D53/50 ,  F01N3/10 ,  B01D50/00

CPC分类号： B01D53/504 ,  B01D2251/404 ,  B03C3/013 ,  B03C3/017 ,  B03C3/16 ,  F23J15/02 ,  F23J15/04 ,  F23J2215/20 ,  F23J2217/102 ,  F23J2219/40

摘要： An object is to provide an exhaust-gas treatment apparatus capable of realizing a dissolved-salt spray method easily and at low cost. An exhaust-gas treatment apparatus that removes SO2 and SO3 contained in combustion exhaust gas includes a desulfurization apparatus based on the lime-gypsum method. Desulfurizing effluent, containing dissolved salt, from the desulfurization apparatus is sprayed to an upstream side of the desulfurization apparatus to remove SO3. A wet electrical dust precipitator may be provided downstream of the desulfurization apparatus. Furthermore, effluent from the wet electrical dust precipitator may be made to merge with the desulfurizing effluent from the desulfurization apparatus.

摘要翻译： 本发明的目的是提供一种能够容易且低成本地实现溶解盐喷雾法的废气处理装置。 除去燃烧废气中所含的SO 2和SO 3的废气处理装置包括基于石灰石膏法的脱硫装置。 将来自脱硫装置的含有溶解盐的脱硫流出物喷雾到脱硫装置的上游侧以除去SO 3。 可以在脱硫装置的下游设置湿式除尘器。 此外，来自湿式电除尘器的流出物可以与来自脱硫装置的脱硫流出物合并。

公开(公告)号：US20060110304A1

公开(公告)日：2006-05-25

申请号：US10523679

申请日：2003-08-06

申请人： Masahiro Harada ,  Shintaro Honjo ,  Makoto Susaki ,  Kazuo Ishida ,  Hajime Nagano ,  Susumu Okino

发明人： Masahiro Harada ,  Shintaro Honjo ,  Makoto Susaki ,  Kazuo Ishida ,  Hajime Nagano ,  Susumu Okino

IPC分类号： B01D53/58

CPC分类号： C10K1/101 ,  B01D53/14 ,  B01D2257/406

摘要： The present invention provides a wet gas purification method in which ammonia in the gas is removed, and a system for carrying out said method, characterized in that the method includes a washing step in which ammonia in the gas is absorbed in an absorbent for removal; and an ammonia treating step in which ammonia is stripped from the discharged absorbent at a following stage of the washing step, wherein the absorbent is divided into an off-gas containing ammonia and effluent. In the washing step makeup water is charged continuously or intermittently so that the concentration of ammonia in the gas having passed through the washing step is 10 ppm or lower. According to the present invention, a wet gas purification method can be performed in which the running costs involved in operation is reduced, the manipulation step and system are simple, operation is easy, and the reliability is high.

摘要翻译： 本发明提供一种其中除去气体中的氨的湿气净化方法，以及用于实施所述方法的系统，其特征在于，所述方法包括洗涤步骤，其中所述气体中的氨被吸收剂吸收除去; 以及在洗涤步骤的后续阶段从排出的吸收剂中除去氨的氨处理步骤，其中吸收剂被分成含有氨和废水的废气。 在洗涤步骤中，连续地或间歇地加入水，使得通过洗涤步骤的气体中的氨浓度为10ppm以下。 根据本发明，可以进行操作中涉及的运行成本降低的操作步骤和系统简单，操作容易，可靠性高的湿气净化方法。

公开(公告)号：US06517792B2

公开(公告)日：2003-02-11

申请号：US09924378

申请日：2001-08-08

申请人： Taku Shimizu ,  Kazuaki Kimura ,  Kiyoshi Okazoe ,  Atsushi Tatani ,  Naohiko Ukawa ,  Masao Hino ,  Susumu Okino ,  Takashi Haruki ,  Toru Takashina ,  Eiji Ochi

发明人： Taku Shimizu ,  Kazuaki Kimura ,  Kiyoshi Okazoe ,  Atsushi Tatani ,  Naohiko Ukawa ,  Masao Hino ,  Susumu Okino ,  Takashi Haruki ,  Toru Takashina ,  Eiji Ochi

IPC分类号： B01D5334

CPC分类号： C10M173/02 ,  B01D53/46 ,  B01D53/501 ,  C10M2215/042 ,  C10M2229/045 ,  C10M2229/046 ,  C10N2220/13 ,  C10N2240/58 ,  F23J15/003 ,  F23J15/022 ,  F23J2215/20 ,  F23J2219/50

摘要： Five combustion exhaust gas treatment systems capable of removing dust and selenium (Se) in combustion exhaust gas and making harmless are proposed: (1) combustion exhaust gas is cooled to 350° C. or less, dust is separated, Se is transformed into insoluble compound, and Se is separated; (2) combustion exhaust gas is cooled to 350° C. or less, dust is separated, Se elution preventive agent is added, and dust is formed into scale; (3) dust in combustion exhaust gas is collected by dust collector, dust is formed into slurry by making use of part of circulation liquid in desulfurization apparatus, and tetravalent Se in dust slurry is transformed into insoluble compound, which is separated into solid and liquid; (4) dust is separated from combustion exhaust gas by dust collector, and it is heated to gasify Se, and is led into desulfurization apparatus, etc., and formed into slurry, and Se is made into insoluble compound; and (5) a treating agent for making tetravalent Se insoluble is added to part of circulation liquid in desulfurization apparatus, and it is sprayed into combustion exhaust gas to make Se insoluble.

公开(公告)号：US5878675A

公开(公告)日：1999-03-09

申请号：US696317

申请日：1996-08-12

申请人： Masaki Iijima ,  Atsushi Tatani ,  Kazuaki Kimura ,  Koichiro Iwashita ,  Satoshi Yajima ,  Toru Takashina ,  Susumu Okino

发明人： Masaki Iijima ,  Atsushi Tatani ,  Kazuaki Kimura ,  Koichiro Iwashita ,  Satoshi Yajima ,  Toru Takashina ,  Susumu Okino

IPC分类号： B01D53/50 ,  F23J15/00 ,  F01K7/34 ,  F22D1/40 ,  F23B7/00

CPC分类号： B01D53/504

摘要： A flue gas desulfurizer having an absorption tower for bringing untreated flue gas into gas-liquid contact with an absorbent slurry, wherein there is provided heat recovery means for recovering heat from the flue gas passing through the flue gas inlet section of the absorption tower prior to gas-liquid contact, and to boiler equipment including heat release means for releasing the recovered heat to heat utilization equipment. This invention also relates to thermal electric power generation equipment including extraction feedwater heaters for heating boiler feedwater with steam from steam turbines, a flue gas desulfurizer using an absorbent slurry, and means for recovering heat from the flue gas passing through the flue gas desulfurizer and/or the absorbent slurry within the flue gas desulfurizer, whereby boiler feedwater is preheated by the recovered heat and then introduced into the extraction feedwater heaters.

摘要翻译： 一种烟道气脱硫器，具有吸收塔，用于将未处理的烟道气与吸收剂浆料气液接触，其中设置有热回收装置，用于在通过吸收塔的烟道气入口部分的烟道气之前回收热量， 气液接触，以及包括用于将回收的热量释放到热利用设备的放热装置的锅炉设备。 本发明还涉及包括用于使用来自蒸汽轮机的蒸汽加热锅炉给水的提取给水加热器，使用吸收剂浆料的烟道气脱硫器和用于从通过烟道气脱硫器的烟道气回收热量的装置的热发电设备和/ 或烟道气脱硫器内的吸收剂浆料，由此锅炉给水由回收的热量预热，然后引入提取给水加热器。

公开(公告)号：US5221298A

公开(公告)日：1993-06-22

申请号：US827216

申请日：1992-01-30

申请人： Eiji Ochi ,  Kiyoshi Okazoe ,  Naohiko Ukawa ,  Susumu Okino ,  Masakazu Onizuka

发明人： Eiji Ochi ,  Kiyoshi Okazoe ,  Naohiko Ukawa ,  Susumu Okino ,  Masakazu Onizuka

IPC分类号： B01D53/50

CPC分类号： B01D53/504 ,  B01D53/501

摘要： A wet exhaust gas desulfurization apparatus includes a housing, an absorbing solution (3, B) stored in the lower portion of the housing, a flue (1, 2, 11, 12, 21, 25) above the surface of the absorbing solution, and a partition plate (4, 15, 25) for dividing the flue into gas inlet and outlet portions. Exhaust gas is introduced as an untreated combustion gas from a space above an absorbing solution (3) divided by a partition plate (4) into the wet exhaust gas desulfurization apparatus, the lower edge (5) of the partition plate is immersed in the solution, pressure of the exhaust gas lowers the upper level (6) of the solution on the upper side of the plate to a level (6') through which the gas passes and flows under the partition plate in contact with the solution leaving the solution on the other side of the plate and then discharges through a space above the absorbing solution on the other side of the partition plate. The plate may be raised and lowered by a rack (4') and pinion ( 4") device, and water jet devices (29) may be used to wash absorbing solution off the surfaces (27, 28) of the plate continuously or intermittently.

公开(公告)号：US4773374A

公开(公告)日：1988-09-27

申请号：US912850

申请日：1986-09-29

申请人： Hideo Kiuchi ,  Oyuki Ogawa ,  Hiroshi Yamazoe ,  Hitoshi Tasaka ,  Minoru Kuroda ,  Susumu Okino

发明人： Hideo Kiuchi ,  Oyuki Ogawa ,  Hiroshi Yamazoe ,  Hitoshi Tasaka ,  Minoru Kuroda ,  Susumu Okino

IPC分类号： F02M51/06 ,  F02M51/08 ,  F02M61/18 ,  F02M69/04 ,  F02M61/06

CPC分类号： F02M61/1826 ,  F02M51/0678 ,  F02M61/1806 ,  F02M69/044 ,  F02M2051/08

摘要： A fuel injector to be mounted on a branch of an engine intake manifold has a hollow body with an injection orifice therein and a valve member mounted slidably in the body and having a pintle extending from one end of the valve member and slidably received in and extending through the injection orifice. A sleeve member is mounted on the body to cover the injection orifice and defines a pintle-receiving space into which the forward end of the pintle extends. Communication apertures are formed in the outer end of the sleeve member to communicate the pintle receiving space with an engine intake passage. The total of the cross-sectional areas of the communication apertures is smaller than the cross-sectional area of the pintle-receiving space.

摘要翻译： 安装在发动机进气歧管的分支上的燃料喷射器具有其中具有喷射孔的中空体和可滑动地安装在主体中的阀构件，并且具有从该阀构件的一端延伸的枢轴并可滑动地容纳在并延伸 通过注射孔。 套筒构件安装在主体上以覆盖注射孔并且限定枢轴接收空间，枢轴的前端延伸到枢轴容纳空间中。 通信孔形成在套筒构件的外端中，以将枢轴接收空间与发动机进气通道连通。 连通孔的横截面面积的总和小于枢轴容纳空间的横截面面积。

公开(公告)号：US4618482A

公开(公告)日：1986-10-21

申请号：US643456

申请日：1984-08-23

申请人： Naoharu Shinoda ,  Atsushi Tatani ,  Setsuo Omoto ,  Susumu Okino ,  Taku Shimizu

发明人： Naoharu Shinoda ,  Atsushi Tatani ,  Setsuo Omoto ,  Susumu Okino ,  Taku Shimizu

IPC分类号： B01D53/50 ,  C01F11/46 ,  C01B17/00 ,  C01F1/00 ,  C01F5/40

CPC分类号： B01D53/501 ,  C01F11/464

摘要： A method for controlling the concentration of a slurry in an absorption tower in which a flue gas comprising SO.sub.2 is brought into contact with a slurry containing suspended Ca compounds therein to absorb the SO.sub.2 with the compounds. The method comprises withdrawing the slurry from the absorption tower in such a way that the slurry is divided into at least two groups with different concentrations, one group being a slurry having a higher concentration of the Ca compound, the other group being a slurry having a lower concentration of the Ca compound, and regulating rates of the slurries being withdrawn from the absorption tower whereby the concentration of the Ca compound in the slurry being contacted with the flue gas is controlled.

摘要翻译： 用于控制吸收塔中的浆料浓度的方法，其中包含SO 2的烟道气与其中含有悬浮的Ca化合物的浆料接触，以吸收化合物的SO 2。 该方法包括从吸收塔中取出浆料，使浆料分成至少两个不同浓度的组，一组是Ca化合物浓度较高的浆料，另一组是具有 较低浓度的Ca化合物，以及从吸收塔中排出的浆料的调节速率，从而控制浆料中与该烟道气接触的Ca化合物的浓度。

公开(公告)号：US4297332A

公开(公告)日：1981-10-27

申请号：US112444

申请日：1980-01-16

申请人： Atsushi Tatani ,  Susumu Okino

发明人： Atsushi Tatani ,  Susumu Okino

IPC分类号： F23J15/04 ,  B01D53/34 ,  B01D53/50 ,  B01D53/77 ,  B09B3/00 ,  C01B7/00

CPC分类号： B01D53/501

摘要： A process for treating an exhaust gas discharged from a coal combustion apparatus, in which the exhaust gas is first led to a dry type dust collecting device, and after fly ash in said exhaust gas is removed, said exhaust gas is treated by a wet type exhaust gas cleaning device; a part of said fly ash collected in said dry type dust collecting device is added to a discharge liquid or a discharge sludge discharged from said wet type exhaust gas cleaning device. The amount of the fly ash to be added to the discharge sludge should be at least three times (in weight) as much as the amount of water contained in said discharge sludge. Preferably fly ash of approximately the same weight as that of said discharge sludge should be added to the discharge sludge discharged from said wet type exhaust gas cleaning device, and subsequently calcium hydroxide of about one-tenth in weight of said discharge sludge should be added to the mixture for solidifying said discharge sludge. In a preferred embodiment, the mixture of the discharge liquid and the fly ash is led to a solid-liquid separator to separate the mixture into clear water and sludge, and the clear water is returned to said wet type exhaust gas cleaning device, while the separated sludge is mixed with additional fly ash to further eliminate a discharge water.

摘要翻译： 一种处理从燃煤装置排出的排气的方法，其中排气首先被引入干式集尘装置，并且在排出所述排气中的飞灰之后，将所述废气用湿式 废气净化装置; 将收集在所述干式集尘装置中的所述飞灰的一部分添加到从所述湿式排气净化装置排出的排出液体或排出污泥中。 添加到排放污泥中的飞灰的量应至少为所述排放污泥中所含的水量的至少三倍（重量）。 优选地，将与所述排放污泥重量大致相等的粉煤灰加入到从所述湿式废气净化装置排出的排放污泥中，随后将所述排放污泥重量的约十分之一氢氧化钙加入 用于固化所述排出污泥的混合物。 在优选的实施方案中，将排出液和飞灰的混合物引入固液分离器，将混合物分离成澄清的水和污泥，并将清水返回到所述湿式废气净化装置，同时 分离的污泥与额外的飞灰混合，以进一步消除排放水。

公开(公告)号：US08992871B2

公开(公告)日：2015-03-31

申请号：US13262848

申请日：2009-04-10

申请人： Toshinobu Yasutake ,  Tetsuya Imai ,  Masanao Yonemura ,  Susumu Okino ,  Keiji Fujikawa ,  Shinya Tachibana

发明人： Toshinobu Yasutake ,  Tetsuya Imai ,  Masanao Yonemura ,  Susumu Okino ,  Keiji Fujikawa ,  Shinya Tachibana

IPC分类号： B01J23/882 ,  B01J21/06 ,  B01J21/12 ,  C01B3/16 ,  C10K3/04 ,  B01J23/887 ,  C01B3/52 ,  C01B3/56 ,  C10K1/02 ,  C10K1/08 ,  C10K1/12 ,  C10J3/00 ,  B01J23/28 ,  B01J23/75 ,  B01J37/00 ,  B01J37/02 ,  B01J37/03

CPC分类号： B01J23/882 ,  B01J21/063 ,  B01J21/066 ,  B01J23/28 ,  B01J23/75 ,  B01J23/8871 ,  B01J37/0009 ,  B01J37/0201 ,  B01J37/0205 ,  B01J37/031 ,  C01B3/16 ,  C01B3/52 ,  C01B3/56 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/06 ,  C01B2203/147 ,  C01B2203/84 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/1618 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10J2300/1687 ,  C10K1/024 ,  C10K1/08 ,  C10K1/12 ,  C10K3/04 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/52

摘要： A CO shift catalyst according to the present invention reforms carbon monoxide (CO) contained in gas. The CO shift catalyst is prepared from one or both of molybdenum (Mo) and cobalt (Co) as an active ingredient and an oxide of one of, or a mixture or a compound of, titanium (Ti), silicon (Si), zirconium (Zr), and cerium (Ce) as a carrier for supporting the active ingredient. The CO shift catalyst can be used in a halogen-resistant CO shift reactor (15) that converts CO contained in gasified gas (12) generated in a gasifier (11) into CO2.

摘要翻译： 根据本发明的CO转化催化剂改变气体中所含的一氧化碳（CO）。 CO转移催化剂由钼（Mo）和钴（Co）中的一种或两种作为活性成分制备，并且钛（Ti），硅（Si），锆之一或其混合物或化合物的氧化物 （Zr）和铈（Ce）作为负载活性成分的载体。 CO转化催化剂可用于将气化器（11）中产生的气化气体（12）中包含的CO转化为CO 2的耐卤化CO转化反应器（15）中。

公开(公告)号：US20120027659A1

公开(公告)日：2012-02-02

申请号：US13262848

申请日：2009-04-10

申请人： Toshinobu Yasutake ,  Tetsuya Imai ,  Masanao Yonemura ,  Susumu Okino ,  Keiji Fujikawa ,  Shinya Tachibana

发明人： Toshinobu Yasutake ,  Tetsuya Imai ,  Masanao Yonemura ,  Susumu Okino ,  Keiji Fujikawa ,  Shinya Tachibana

IPC分类号： B01D53/62 ,  B01J23/882 ,  B01J21/08 ,  B01J21/06 ,  B01J21/12

CPC分类号： B01J23/882 ,  B01J21/063 ,  B01J21/066 ,  B01J23/28 ,  B01J23/75 ,  B01J23/8871 ,  B01J37/0009 ,  B01J37/0201 ,  B01J37/0205 ,  B01J37/031 ,  C01B3/16 ,  C01B3/52 ,  C01B3/56 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/06 ,  C01B2203/147 ,  C01B2203/84 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/1618 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1678 ,  C10J2300/1687 ,  C10K1/024 ,  C10K1/08 ,  C10K1/12 ,  C10K3/04 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/52

摘要： A CO shift catalyst according to the present invention reforms carbon monoxide (CO) contained in gas. The CO shift catalyst is prepared from one or both of molybdenum (Mo) and cobalt (Co) as an active ingredient and an oxide of one of, or a mixture or a compound of, titanium (Ti), silicon (Si), zirconium (Zr), and cerium (Ce) as a carrier for supporting the active ingredient. The CO shift catalyst can be used in a halogen-resistant CO shift reactor (15) that converts CO contained in gasified gas (12) generated in a gasifier (11) into CO2.

摘要翻译： 根据本发明的CO转化催化剂改变气体中所含的一氧化碳（CO）。 CO转移催化剂由钼（Mo）和钴（Co）中的一种或两种作为活性成分制备，并且钛（Ti），硅（Si），锆之一或其混合物或化合物的氧化物 （Zr）和铈（Ce）作为负载活性成分的载体。 CO转化催化剂可用于将气化器（11）中产生的气化气体（12）中包含的CO转化为CO 2的耐卤化CO转化反应器（15）中。