公开(公告)号：US09982552B2

公开(公告)日：2018-05-29

申请号：US14764365

申请日：2014-01-27

Applicant: Tsukishima Kikai Co., Ltd. ,  Sanki Engineering Co., Ltd.

Inventor： Ken Nakano ,  Yutaka Hirata ,  Yuki Asaoka ,  Kazuyoshi Terakoshi ,  Toshiki Kobayashi ,  Takafumi Yamamoto ,  Takamitsu Kanno ,  Kunihiko Koga ,  Tomokazu Suyama

IPC: F01D11/04 ,  F23L5/02 ,  F23C10/18 ,  F23C10/16 ,  F23G5/30

CPC classification number: F01D11/04 ,  F05D2220/40 ,  F23C10/16 ,  F23C10/18 ,  F23G5/30 ,  F23G2200/00 ,  F23G2202/30 ,  F23G2203/502 ,  F23L5/02 ,  F23L2900/05021

Abstract: A pressurized incineration facility (100, 200) includes: a pressurized incinerator (1) which incinerates a processing object (P) under a pressure increased by compressed air (A); a turbocharger (5) which produces the compressed air by being rotationally driven by combustion exhaust gas (G) of the pressurized incinerator; and a seal device (5i) which jets seal gas (S) to a rear surface (5a1) of a turbine impeller (5a) of the turbocharger.

公开(公告)号：US09897376B2

公开(公告)日：2018-02-20

申请号：US15125443

申请日：2015-06-01

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Yoichi Nakata ,  Sumito Sato ,  Satoshi Suwa ,  Tomonori Watarai

IPC: F26B17/32 ,  F26B25/00 ,  F26B3/02 ,  C10L5/04 ,  C10L9/08

CPC classification number: F26B17/32 ,  C10L5/04 ,  C10L9/08 ,  C10L2290/08 ,  F26B3/02 ,  F26B3/20 ,  F26B3/22 ,  F26B23/10 ,  F26B25/001

Abstract: To provide a drying method for processing material and a horizontal rotary dryer allowing easy performance of mass processing of the processing material and enabling size reduction by improving drying performance of the dryer. In a drying method for processing material in which a horizontal rotary dryer provided with: a rotating shell having a feed port for processing material on one end side thereof and a discharge port for processing material on the other end side thereof, and capable of freely rotating around an axial center; and a group of heating tubes through which a heating medium passes, provided within the rotating shell, and configured in a manner that the processing material is lifted up in a rotational direction by the group of heating tubes in accordance with the rotation of the rotating shell, is used, and the processing material is dried, through indirect heating, by using the group of heating tubes in a process of feeding the processing material to the one end side of the rotating shell and discharging the processing material from the other end side of the rotating shell, the rotating shell is rotated to make a critical speed ratio α defined by the following expression 1 and expression 2 become 30 to less than 100% to dry the processing material, Vc=2.21D1/2  Expression 1 α=V/Vc·100  Expression 2 wherein Vc indicates a critical speed (m/s), D indicates an inside diameter (m) of the rotating shell, α indicates the critical speed ratio (%), and V indicates a rotation speed (m/s).

公开(公告)号：US20150322398A1

公开(公告)日：2015-11-12

申请号：US14409404

申请日：2013-03-27

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Tomoki HAYAKAWA ,  Hideaki MIZUNO

IPC: C12M1/00 ,  C12M1/34 ,  C12P19/14 ,  C12P7/10 ,  C12P7/56 ,  C12P7/46 ,  C12M1/12 ,  C12P19/02

CPC classification number: C12M23/58 ,  C12M21/18 ,  C12M29/18 ,  C12M37/00 ,  C12M41/44 ,  C12M45/06 ,  C12M45/20 ,  C12P7/10 ,  C12P7/46 ,  C12P7/56 ,  C12P19/02 ,  C12P19/14 ,  C12P2201/00 ,  C12P2203/00 ,  Y02E50/16

Abstract: A biomass treatment device and a biomass treatment method, in which contamination is prevented and a final product can be highly concentrated. The biomass treatment device includes a pretreatment device for pretreating a biomass, a slurrying device for slurrying the pretreated biomass, and a saccharification device for saccharifying the slurried biomass with a saccharifying enzyme. A return line for returning a part of an internal fluid in the saccharification device to the slurrying device is provided, and the pretreated biomass from the pretreatment device and the internal fluid returned through the return line are mixed in the slurrying device so as to generate biomass slurry.

Abstract translation: 一种生物质处理装置和生物处理方法，其中防止污染并且最终产品可以高度浓缩。 生物质处理装置包括用于预处理生物质的预处理装置，用于使预处理的生物质浆化的制浆装置，以及用糖化酶对浆化的生物质进行糖化的糖化装置。 提供了用于将糖化装置中的一部分内部流体返回到浆料装置的返回管线，并且将来自预处理装置的预处理生物质和通过返回管线返回的内部流体在制浆装置中混合以产生生物质 泥浆。

公开(公告)号：US20150217264A1

公开(公告)日：2015-08-06

申请号：US14423045

申请日：2013-02-25

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Yo Doya ,  Hidenori Goto

IPC: B01J19/24 ,  B01J19/18

CPC classification number: B01J19/24 ,  B01F3/0853 ,  B01F3/0865 ,  B01F5/0065 ,  B01F5/0071 ,  B01F5/10 ,  B01F7/18 ,  B01F13/1016 ,  B01F13/1022 ,  B01F15/065 ,  B01J19/1862 ,  B01J19/2405 ,  B01J19/242 ,  B01J19/2435 ,  B01J2219/2401 ,  C01G53/006 ,  C01P2004/03

Abstract: To provide a processing device which is small but which can exhibits a sufficient processing amount and a uniform contact processing property. In the processing vessel 10, a liquid flow is set to a spiral flow, and in a contact processing field, the injection liquid A, B are injected at a center-side position with respect to an inner surface of the processing vessel so as to perform contact processing.

Abstract translation: 为了提供一种处理装置，其处理量小，并具有均匀的接触处理性能。 在处理容器10中，液流被设定为螺旋流，在接触处理场中，喷射液A，B相对于处理容器的内表面在中心侧位置喷射， 执行联系处理。

公开(公告)号：US20150188133A1

公开(公告)日：2015-07-02

申请号：US14409347

申请日：2013-02-15

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Yo Doya ,  Hidenori Goto

IPC: H01M4/505 ,  H01M4/525 ,  C01G53/06 ,  B01J19/24 ,  C01G53/04 ,  H01M10/0525 ,  H01M4/58

CPC classification number: H01M4/505 ,  B01D9/0009 ,  B01D9/0036 ,  B01D9/004 ,  B01J8/14 ,  B01J19/18 ,  B01J19/1806 ,  B01J19/2405 ,  B01J19/245 ,  B01J19/2465 ,  B01J2208/003 ,  B01J2219/0011 ,  B01J2219/00114 ,  B01J2219/00164 ,  B01J2219/24 ,  C01G53/006 ,  C01G53/04 ,  C01G53/06 ,  C01P2004/03 ,  H01M4/525 ,  H01M4/5825 ,  H01M10/0525 ,  H01M2004/028

Abstract: Liquid flow in a reaction processing vessel 10 is set to a spiral flow, a liquid A and B as an additional liquid containing an inorganic substance to be added is injected at a center-side position with respect to an inner surface of the reaction processing vessel 10 in a reaction field of the reaction processing vessel 10 so as to perform reaction processing.

Abstract translation: 将反应处理容器10中的液体流量设定为螺旋流量，将作为附加液体的液体A和B作为附加液体注入相对于反应处理容器的内表面的中心位置 10在反应处理容器10的反应场中进行反应处理。

公开(公告)号：US10279287B2

公开(公告)日：2019-05-07

申请号：US15110538

申请日：2014-12-22

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Yoichi Nakata ,  Tomonori Watarai ,  Sumito Sato ,  Satoshi Suwa ,  Tomoki Homma

IPC: B01D33/64 ,  F26B17/02 ,  B01D33/66 ,  F26B5/14 ,  F26B17/32 ,  F26B17/28

Abstract: Prevention of contamination of a dried product, deformation of particles, and a change of particle size distribution. The system includes: a solid-liquid separator in which a processing material is supplied between a pair of endless separation filter cloths wound around an outer periphery of a separation roll, and is dehydrated by being squeezed therebetween and also by ventilation gas passing from a ventilation port formed in an outer peripheral surface of the separation roll; and a horizontal rotary dryer provided on a subsequent stage of the solid-liquid separator, wherein carrier gas is made to flow in a rotating shell of the dryer in a cocurrent manner in the same direction as a conveyance direction of the processing material.

公开(公告)号：US20180187974A1

公开(公告)日：2018-07-05

申请号：US15123561

申请日：2015-12-09

Applicant: TSUKISHIMA KIKAI CO., LTD.

Inventor： Yoichi NAKATA ,  Yuichi ONO ,  Satoshi SUWA ,  Sumito SATO

IPC: F26B17/32

CPC classification number: F26B17/32 ,  F26B3/24 ,  F26B23/10

Abstract: To provide a drying method for terephthalic acid and a horizontal rotary dryer allowing easy performance of mass processing of the terephthalic acid and enabling size reduction by improving drying performance of the dryer. In a method of drying terephthalic acid by using a horizontal rotary dryer, a rotating shell is rotated to make a critical speed ratio α defined by expression 1 and expression 2 become 17 to less than 80% to dry the processing material, Vc=2.21D1/2   Expression 1 α=V/V c·100   Expression 2 wherein Vc indicates a critical speed (m/s) of the rotating shell, D indicates an inside diameter (m) of the rotating shell, α indicates the critical speed ratio (%) of the rotating shell, and V indicates a rotation speed (m/s) of the rotating shell.

公开(公告)号：US10001277B2

公开(公告)日：2018-06-19

申请号：US14386736

申请日：2013-03-22

Applicant: TSUKISHIMA KIKAI CO., LTD. ,  SANKI ENGINEERING CO., LTD.

Inventor： Takamitsu Kanno ,  Kazuyoshi Terakoshi ,  Takafumi Yamamoto ,  Kunihiko Koga ,  Tomokazu Suyama ,  Isamu Orito

IPC: F23J15/02 ,  F23C10/08 ,  F23C10/16 ,  F23J3/00 ,  F23C10/00 ,  F23G5/44 ,  F23G5/30

CPC classification number: F23J15/022 ,  F23C10/002 ,  F23C10/08 ,  F23C10/16 ,  F23G5/30 ,  F23G5/44 ,  F23G2203/50 ,  F23G2203/501 ,  F23G2209/30 ,  F23J3/00 ,  F23J15/027

Abstract: A method for efficiently conveying impurities in a pressurized fluidized incinerator system is provided. Cleaning gas is supplied to an upper valve, and thereafter, the upper valve is driven so as to communicate an upper discharge device and a tank. The upper discharge device is driven so as to convey the impurities from the dust collector to the tank, and thereafter, the upper discharge device is stopped and the upper valve is driven so as not to communicate the upper discharge device and the tank. Thereafter, the supply of the cleaning gas to the upper valve is stopped.

公开(公告)号：US09933156B2

公开(公告)日：2018-04-03

申请号：US14777797

申请日：2014-02-14

Applicant: Tsukishima Kikai Co., Ltd.

Inventor： Toshiki Kobayashi ,  Takafumi Yamamoto ,  Kazuyoshi Terakoshi

IPC: F23C10/16 ,  F23J15/00 ,  F23J15/06 ,  F23L15/04 ,  F23G5/30

CPC classification number: F23C10/16 ,  F23G5/30 ,  F23G2202/30 ,  F23G2209/12 ,  F23J15/006 ,  F23J15/06 ,  F23J2217/101 ,  F23J2217/103 ,  F23J2217/104 ,  F23J2219/40 ,  F23J2900/15004 ,  F23L15/04 ,  F23L2900/05021 ,  Y02E20/348

Abstract: Pressurized fluidized furnace equipment includes a fluidized bed furnace (1) that pressurizes combustion air (B) and combusts a material to be treated (A) while fluidizing the same; an air preheater (3) that exchanges heat between a combustion exhaust gas (C) discharged from the fluidized bed furnace (1) and the combustion air (B); a dust collector (4) that removes dust from the combustion exhaust gas (C); and first and second superchargers (5, 6) to which the combustion exhaust gas (C), having undergone the heat exchange in the air preheater (3) and the dust removal in the dust collector (4), is supplied to generate compressed air (D, E). The first compressed air (D) generated in the first supercharger (5) is supplied as the combustion air (B) to the fluidized bed furnace (1) by way of the air preheater (3), and the second compressed air (E) generated in the second supercharger (6) is made to have a higher pressure than that of the first compressed air (D). Accordingly, it is possible to prevent the equipment from having more superchargers than is necessary for normal use although a plurality of first and second superchargers are provided, and to efficiently use the surplus combustion exhaust gas.

公开(公告)号：US09758630B2

公开(公告)日：2017-09-12

申请号：US15127035

申请日：2015-03-27

Applicant: TEIJIN LIMITED ,  TSUKISHIMA KIKAI CO., LTD.

Inventor： Tatsuichirou Kon ,  Tatsuya Ekinaka ,  Hiroshi Kishimoto ,  Yume Morita ,  Takehiro Suga ,  Satoshi Ogata ,  Masato Nakagomi

IPC: C08J7/04 ,  C08J7/12 ,  B05D3/02 ,  C23C16/40 ,  C23C16/50 ,  C23C16/02

CPC classification number: C08J7/045 ,  B05D3/0254 ,  B05D7/02 ,  C08J7/047 ,  C08J7/123 ,  C08J2369/00 ,  C08J2433/08 ,  C08J2483/04 ,  C09D183/04 ,  C23C16/02 ,  C23C16/0254 ,  C23C16/0272 ,  C23C16/401 ,  C23C16/402 ,  C23C16/45565 ,  C23C16/45572 ,  C23C16/50 ,  C23C16/5096 ,  C23C16/56 ,  C23C18/122 ,  C23C18/1233 ,  C23C18/1254 ,  H01J37/32091 ,  C08K3/36

Abstract: The present invention realizes a polymer substrate with hard coating layer comprising a high level of environmental resistance and a high level of abrasion resistance.A polymer substrate with hard coating layer is provided that comprises a polymer substrate (60) having a thickness of 1 mm to 20 mm and a hard coating layer (70,80) on the surface thereof. Here, in this polymer substrate with hard coating layer, the hard coating layer (70,80) is laminated on the surface of the polymer substrate, contains as a main component thereof a hydrolysis-condensation product of an organic silicon compound, has a thickness of 0.1 μm to 20 μm, makes direct contact with a cured underlayer on the opposite side of the polymer substrate, is formed from an organic silicon compound by PE-CVD, and satisfies all of the following requirements (a) to (c): (a) film thickness of the silicon oxide layer is within the range of 3.5 μm to 9.0 μm, (b) maximum indentation depth of the surface of the silicon oxide layer as determined by measuring nanoindentation under conditions of a maximum load of 1 mN is 150 nm or less, and (c) the value of critical compression ratio K of the silicon oxide layer, as defined by formula (1) in a 3-point bending test of the polymer substrate with hard coating layer that imparts indentation displacement in which the surface laminated with the silicon oxide layer becomes concave, is 0.975 or less.