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1. 发明专利

JP2008062136A Exhaust gas treatment method and device 审中-公开
标题翻译：排气处理方法和装置
公开(公告)号：JP2008062136A
公开(公告)日：2008-03-21
申请号：JP2006240472
申请日：2006-09-05
申请人： Babcock Hitachi Kk , バブコック日立株式会社
发明人： ISHIOKA MASAAKI , NAGAI YOSHINORI , MORI YOSHIMICHI
IPC分类号： B01D53/86 , B01D53/56 , B01D53/64 , B01D53/70 , B01D53/74 , B01D53/94 , B01J23/28 , B01J23/30
摘要： PROBLEM TO BE SOLVED: To provide an exhaust gas treatment method and device using a catalyst for lowering the concentration of NOx in exhaust gas at a high reducing rate without lowering a DXNs decomposition rate or a mercury oxidation rate. SOLUTION: A catalytic device reduces NOx in exhaust gas using NH 3 injected into the exhaust gas, and at the same time, decomposes DXNs in the exhaust gas using NO 2 in the exhaust gas, or oxidizes Hg in the exhaust gas using NO 2 in the exhaust gas, wherein an upper limit value of an injection amount of NH 3 determined from a molar ratio of NH 3 /NOx is set so that the molar ratio of NH 3 /NOx is less than 1.0. COPYRIGHT: (C)2008,JPO&INPIT
摘要翻译：解决问题：提供一种废气处理方法和装置，其使用催化剂，以降低废气中的NOx浓度降低，而不会降低DXN分解速率或汞氧化速率。解决方案：催化装置使用注入废气的NH 3 SB 3还原废气中的NOx，同时使用NO SB SB2分解废气中的DXN 在排气中使用NO 2 在废气中氧化Hg，其中，从废气中确定的NH 3 的喷射量的上限值设定NH 3 SB 3 / NO x的摩尔比使得NH 3 SBS / NO x的摩尔比小于1.0。版权所有（C）2008，JPO＆INPIT

2. 发明专利

JP2006122878A Exhaust gas denitrification system and method 有权
标题翻译：排气净化系统及方法
公开(公告)号：JP2006122878A
公开(公告)日：2006-05-18
申请号：JP2004318243
申请日：2004-11-01
申请人： Babcock Hitachi Kk , バブコック日立株式会社
发明人： MORI YOSHIMICHI
IPC分类号： B01D53/56 , B01D53/94 , F01N3/08 , F01N3/22
摘要： PROBLEM TO BE SOLVED: To provide an urea water supplying system capable of simply and economically preventing the inside of an urea water spraying nozzle from clogging. SOLUTION: In the system, in order to stop the supply of urea water from an urea water supplying line 10 to an exhaust gas duct 3 while stopping an urea water supplying pump 6, a cut-off valve 8 is installed in the urea water supplying line 10 right before the urea water spraying nozzle 4 at the tip of the line 10, and the cut-off valve 8 is closed while stopping the pump 6. In addition, an urea water drainage line 11 for releasing the residual pressure of an air chamber 9 for pulsation prevention disposed in the outlet of the pump 6 is installed in parallel to the line 10 so as to make a detour from the pump 6 and the air chamber 9, and a cut-off valve 12 of the urea water drainage line 11 is made open while stopping the pump 6 to make the urea water flow to a low pressure part of the inlet of the pump 6. COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：提供一种能够简单且经济地防止尿素水喷雾喷嘴内部堵塞的尿素水供给系统。解决方案：在系统中，为了在停止尿素水供给泵6的同时停止将尿素水从尿素水供给管线10供给到排气管道3，截止阀8安装在尿素水供给管线10在尿素水喷射喷嘴4正前方的管线10的前端，截止阀8在停止泵6的同时关闭。此外，还具有用于释放残留压力的尿素水排出管路11 设置在泵6的出口中的用于防止脉动防止的空气室9与管线10平行地安装，以便从泵6和空气室9绕行，以及尿素的截止阀12 排水管路11在停止泵6时使尿素水流入泵6的入口的低压部分而打开。（C）2006年，JPO＆NCIPI

3. 发明专利

JP2005211750A Method for controlling ammonia injection into catalytic denitrification equipment 审中-公开
标题翻译：控制氨态氮注入催化降解设备的方法
公开(公告)号：JP2005211750A
公开(公告)日：2005-08-11
申请号：JP2004019848
申请日：2004-01-28
申请人： Babcock Hitachi Kk , バブコック日立株式会社
发明人： ISHIOKA MASAAKI , MORITA ISATO , MORI YOSHIMICHI , TERAYAMA FUMIO
IPC分类号： B01D53/56 , B01D53/34 , B01D53/74 , B01D53/94
摘要： PROBLEM TO BE SOLVED: To provide a method for controlling NH 3 (ammonia) injection into catalytic denitrification equipment capable of inexpensively controlling the NH 3 injection so as to keep the outlet concentration of NO X constant with a small variation range. SOLUTION: In the method for controlling NH 3 injection into catalytic denitrification equipment, NO X in waste gas discharged from a waste incinerator is removed by an ammonia catalytic reduction method. Therein, the upper limit, intermediate and lower limit values of ammonia quantity injected into the inlet of the catalytic denitrification equipment and the outlet concentration of NO X of the catalytic denitrification equipment are set beforehand. When the measured value of the outlet concentration of NO X of the catalytic denitrification equipment exceeds the set value of the outlet concentration of NO X , the NH 3 quantity in the range calculated from the deviation of the outlet concentration of NO X and the set value of the outlet concentration of NO X and between the upper limit value and the intermediate value is injected instantly and pulsatively to the inlet of the catalytic denitrification equipment, and the outlet concentration of NO X of the catalytic denitrification equipment is kept constant. When the measurement of the outlet concentration of NO X of the catalytic denitrification equipment is smaller than the set value of the outlet concentration of NO X , the ammonia quantity in the range calculated from the deviation of the outlet concentration of NO X and the set value of the outlet concentration of NO X and between the intermediate value and the lower limit value is injected instantly and pulsatively to the inlet of the catalytic denitrification equipment and the outlet concentration of NO X of the catalytic denitrification equipment is kept constant. COPYRIGHT: (C)2005,JPO&NCIPI
摘要翻译：要解决的问题：提供一种控制NH 3 SB（氨）注入到能够廉价地控制NH 3 SB 3注射的催化脱氮设备中的方法，以便保持 NO X 的出口浓度变化范围小。解决方案：在用于控制NH 3 SB 3注射到催化脱氮设备中的方法中，通过氨催化还原法除去废物焚烧炉排出的废气中的NOS SB 。其中，预先设定了催化脱氮装置的入口的氨量的上限，中下限值和催化脱氮装置的NO X 的出口浓度。当催化脱氮设备的NO X 的出口浓度的测量值超过NO X 的出口浓度的设定值时，NH SB>根据NO X 的出口浓度的偏差和NO X 的出口浓度的设定值计算的范围内的数量，以及上限值和中间值立即和脉动地注入催化反硝化设备的入口，并且催化脱氮设备的NO X 的出口浓度保持恒定。当催化反硝化设备的NO X 的出口浓度的测量值小于NO X 的出口浓度的设定值时，计算的范围内的氨量从NO X 的出口浓度的偏差和NO X 的出口浓度的设定值和中间值与下限值之间立即和脉动地注入到催化脱氮设备的入口和催化脱氮设备的NO X 的出口浓度保持恒定。版权所有（C）2005，JPO＆NCIPI

4. 发明专利

JP2002224532A FLUE GAS TREATMENT METHOD AND SYSTEM THEREFOR 失效
公开(公告)号：JP2002224532A
公开(公告)日：2002-08-13
申请号：JP2001024333
申请日：2001-01-31
申请人： BABCOCK HITACHI KK
发明人： NAGAI YOSHINORI , FUJIWARA TADAYUKI , SATO NAOYUKI , MORI YOSHIMICHI , MORITA ISATO
IPC分类号： F23J15/06 , B01D53/34 , B01D53/50 , B01D53/68 , B01D53/77 , B01D53/86 , B03C3/02 , F23J15/00 , F23J15/04 , F23J15/08
摘要： PROBLEM TO BE SOLVED: To provide a method for efficiently and economically treating a flue gas discharged from an incineration apparatus for municipal refuses or industrial wastes. SOLUTION: A flue gas discharged from an incineration apparatus for municipal refuses, industrial wastes, etc., is subjected to temperature decrease with a boiler 11 and a gas-cooling tower and then is subjected to dust removal with a dust collector 12. At the downstream side of the dust collector 12, a corrosion- resistant heat exchanger 13 and then a wet-type smoke-cleaning apparatus 15 are installed. After the flue gas at the outlet of the smoke-cleaning apparatus 15 is introduced into the heat exchanger 13 to be subjected to heat exchange, the gas is supplied to a catalyst tower 17, if necessary through a flue gas heater 16. Since the heat exchanger installed at the downstream side of the dust removal uses tubes made of corrosion-resistant glass, the exchanger is resistant to an acidic gas. Since the flue gas supplied to the catalyst tower is subjected to heat exchange with the flue gas of a relatively high temperature before the temperature decrease, treatment efficiency can be elevated. Thus, the amount of steam used can be decreased to a large extent.

5. 发明专利

JPH02198623A MOVING-BED REACTOR PROVIDED WITH FLOW STRAIGHTENING BODY FOR MOVING-BED GRAINS AND ITS FABRICATION METHOD 失效
公开(公告)号：JPH02198623A
公开(公告)日：1990-08-07
申请号：JP1496489
申请日：1989-01-26
申请人： BABCOCK HITACHI KK
发明人： WADA TOSHIMICHI , MORI YOSHIMICHI
IPC分类号： B01D53/08 , B01D15/02 , B01D53/86 , B01J8/12
摘要： PURPOSE:To uniformly move the moving-method grains by providing a flow straightening body for moving-bed grains with a fixed apex angle at the upper and lower parts and having an almost rhombic section practically on the center line of the moving bed in the vicinity of the boundary between the moving bed and hopper part. CONSTITUTION:Grains are continuously supplied to the moving bed 4 and brought into countercurrent or cocurrent contact with a fluid, and various reactions are carried in out in the moving bed 4. The hopper part 1 for discharging the grains is also provided. The rhombic flow straightening body 3 with an apex angle of (90-theta)X2+ or -5 deg. (theta is the angle of the inclined hopper part to the horizontal direction and is smaller than 90 deg.) at the upper and lower parts is provided in the bed 4 practically on the center line of the bed 4 in the vicinity of the boundary between the bed 4 and hopper par 1 as the means for preventing the formation of an immobilized region or as the means for minimizing the formation of the region. As a result, the moving pattern of the moving- bed grains is practically uniformized, and the reaction efficiency in various reaction systems is significantly improved.

6. 发明专利

JPS5794341A BLOCK CATALYTIC DEVICE 失效
公开(公告)号：JPS5794341A
公开(公告)日：1982-06-11
申请号：JP17023480
申请日：1980-12-04
申请人： BABCOCK HITACHI KK
发明人： MORI YOSHIMICHI
IPC分类号： B01D53/86 , B01J8/00 , B01J19/24
摘要： PURPOSE:To prevent gas leak and increase efficiency of catalytic reaction by using two kinds, large and small, of catalyst blocks and setting the lapped catalyst blocks out of alignment. CONSTITUTION:In an catalytic device in which row of catalyst blocks 4 containing many catalysts in a frame 3 are arranged in plural rows in the direction of gas flow, dimension of a marginal catalyst block 4 out of the row of the same catalyst blocks 4 is made different from others, and this catalyst block 4 of different dimension is placed at different margin in adjoining rows of catalyst blocks 4. By constituting a catalytic device with such catalyst blocks 4, gas leak can be prevented and efficiency of catalytic reaction can be increased.

7. 发明专利

JPS5768134A Fixing device of reactor 失效
标题翻译：固定反应器装置
公开(公告)号：JPS5768134A
公开(公告)日：1982-04-26
申请号：JP14245380
申请日：1980-10-14
申请人： Babcock Hitachi Kk
发明人： MORI YOSHIMICHI , YUKI MASAHARU
IPC分类号： B01D53/86 , B01J8/00 , B01J19/24
CPC分类号： B01J8/008 , B01J19/2485 , B01J2208/00814
摘要： PURPOSE:To provide a fixing device which controls the displacement of a reactor by horizontal force easily by placing an imaginary fixing point at the center of the reactor, and controlling the plugs profected from the respective beams in the four sides in the lowermost part of the reactor by means of stoppers provided to the respective beams of a stand from both sides. CONSTITUTION:Lugs 8 for stoppers are projected to the central parts of the beams 7 at four sides in the bottom part of the reator, and stoppers 10 controlling movement in the longitudianl direction of the beam of the lugs 8 are provided in the central parts of beams 9 of a stand on both sides of the lugs 8. The gaps (overlap parts) of the stoppers 10 and the lugs 8 are set suitably in consideration for thermal expansion of the reactor, for example, at about 50-100mm.. With the above- mentioned constitution, when horizontal force such as seismic force, wind pressure or the like is applied upon the reactor, the lugs 8 abut on the stoppers 10, thereby controlling the displacement of the reactor by the horizontal force. When horizontal force in, for example, an X direction, is exerted, the lugs 8 abut on the stoppers at the points D, E, thereby controlling the displacement of the reactor. Since the respective displacement control parts are provided to the beams on the four sides, the reactor assumes the same state as that of the provision of a fixed point at the center A and the reactor is fixed to the stand surely.
摘要翻译：目的：提供一种定影装置，其通过将假想固定点放置在反应堆的中心处，容易地通过水平力控制反应堆的位移，并且控制从位于反应堆的最下部分的四个侧面中的各个横梁的插头反应器通过从两侧设置到支架的各个梁的止动件。构成：用于止动件的凸耳8在转子的底部的四侧投射到梁7的中心部分，并且控制凸耳8的梁的纵向方向上的移动的止动件10设置在考虑到反应器的热膨胀，止动件10和凸耳8的间隙（重叠部分）适当地设定在例如约50-100mm处。对于上述结构，当在反应堆上施加诸如地震力，风压等的水平力时，凸耳8抵靠在止动件10上，从而通过水平力来控制反应器的位移。当施加例如X方向的水平力时，凸耳8在点D，E处邻接止动件，从而控制反应器的位移。由于各个位移控制部分设置在四侧的梁上，所以反应器呈现与设置在中心A处的固定点相同的状态，反应器可靠地固定在支架上。

8. 发明专利

JPS56141852A WASTE GAS TREATING APPARATUS 失效
公开(公告)号：JPS56141852A
公开(公告)日：1981-11-05
申请号：JP4287680
申请日：1980-04-03
申请人： BABCOCK HITACHI KK
发明人： WATANABE SHIGEO , MORITA TAKETO , MORI YOSHIMICHI
IPC分类号： B01D53/94 , B03C3/01 , B03C3/013
摘要： PURPOSE:To prevent corrosion of a heat exchanger and improve the dust collection efficiency of an electrical dust precipitator by providing an SO2 conversion reactor and the heat exchanger to the flow-rate-controllable bypass provided to the main pipeline to the electrical dust precipitator for dust-laden waste combustion gases. CONSTITUTION:NH3 from an NH3 injecting device 2 is added to the waste gas from a combustion apparatus 1, and NOx is denitrated in a denitrating device 3 for reduction. Part of the waste gas after the denitration is introduced via a damper 9 into a conversion reactor 8, where SO2 is converted to SO3, after which the gas is returned via a secondary air preheater 10 to the front flow of an electrical dust precipitator 5. The gas flows of the main pipeline and bypass pipeline are controlled with the damper 9 so that the SO3 supplied to the dust precipitator 5 attains a proper amount. On the other hand, air is preheated in a primary air preheater 11, after which it is conducted through a pipeline 12 into the preheater 10. In this way, the gas temperatures of the air preheaters 10, 11 are maintained higher than dew point of acid, whereby condensation, etc. of acids are avoided and corrosion is prevented.

9. 发明专利

JP2011163304A Duct seal structure and method for forming the same seal structure 有权
标题翻译： DUCT密封结构和形成相同密封结构的方法
公开(公告)号：JP2011163304A
公开(公告)日：2011-08-25
申请号：JP2010029945
申请日：2010-02-15
申请人： Babcock Hitachi Kk , バブコック日立株式会社
发明人： MORI YOSHIMICHI , MASUTOMI HIROSHI , MORII SEIJI , SERA KAZUHIKO
IPC分类号： F01N13/08 , B01D53/86 , B01D53/94 , F01D25/30 , F01N13/18 , F02C7/28 , F16J15/00 , F16J15/08
摘要： PROBLEM TO BE SOLVED: To provide a duct seal structure and a method for attaching the duct seal structure easily adjustable at the site where HRSG is installed, and surely sealing gas.
SOLUTION: A sealing device 1 prepared by stacking a plurality of hard-to-rust metal thin plates is held by a sealing device attachment plate 5 having a stud bolt 3 and a sealing device pressing plate 2, and the stud bolt 3 protruding from the pressing plate 2 is fastened by a nut 4, and the sealing device 1 is attached between the attachment plate 5 and the pressing plate 2, and a seal surface forming plate 6 is combined in a dimension for exhibiting a function of the sealing device 1 so that the other side of the sealing device 1 having one side supported by the attachment plate 5 and the pressing plate 2 contacts thereto, and the attachment plate 5 and the forming plate 6 are fixed by a stay 7, and the stay is removed after being attached to a seal forming part in the installation site. Thus, the sealing device having a width capable of sufficiently absorbing the site assembly dimension error can be obtained, and adjusting work of the seal part at the site can be dispensed with, and quality is enhanced.
COPYRIGHT: (C)2011,JPO&INPIT
摘要翻译：要解决的问题：提供一种管道密封结构和一种在安装HRSG的位置处容易调节的管道密封结构的安装方法，并确保密封气体。解决方案：通过堆叠多个难锈蚀金属薄板制备的密封装置1由具有双头螺栓3和密封装置按压板2的密封装置安装板5保持，并且双头螺栓3 从压板2突出的螺母4由螺母4紧固，密封装置1安装在安装板5和按压板2之间，密封面形成板6的组合尺寸为密封性装置1，使得由安装板5支撑的一侧的密封装置1的另一侧与按压板2接触，并且安装板5和成形板6通过支柱7固定，在安装在安装地点的密封件形成部件之后移除。因此，可以获得能够充分吸收现场组装尺寸误差的宽度的密封装置，并且可以省去现场的密封部的调整作业，提高质量。版权所有（C）2011，JPO＆INPIT

10. 发明专利

JP2002021579A METHOD OF CONTROLLING COMBINED CYCLE PLANT PROVIDED WITH GAS TURBINE AND MUST-HEAT RECOVERY BOILER, AND CONTROLLER THEREFOR 失效
公开(公告)号：JP2002021579A
公开(公告)日：2002-01-23
申请号：JP2000205440
申请日：2000-07-06
申请人： BABCOCK HITACHI KK
发明人： MORI YOSHIMICHI , INATSUNE YOSHIROU , WATANABE KO
IPC分类号： F01K23/10 , F02C6/18 , F02C7/057 , F02C9/54
摘要： PROBLEM TO BE SOLVED: To provide a control method by which an NOX discharge amount discharged from a plant is prevented from exceeding a regulatory value even when an exhaust temperature is low in start-up of the plant, in the combined cycle plant combined with a gas turbine and an exhaust-heat recovery boiler. SOLUTION: When the combined cycle plant provided with the gas turbine 1 for driving a generator 15 the recovery boiler 3 for gas turbine exhaust, and a denitration equipment 6 built in the boiler is started up, a moving vane angle of a compressor 11 is controlled to bring the NOX discharge amount discharged from the plant into the regulatory value or less until a detected value by an exhaust gas thermometer 24 in an inlet of the denitration equipment reaches to a temperature suitable for denitraion, so as to reduce an intervane passage width, and an exhaust gas amount flowing from the gas turbine into the denitration equipment is reduced thereby to a prescribed amount or less.

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