公开(公告)号：US20180169058A1

公开(公告)日：2018-06-21

申请号：US15895197

申请日：2018-02-13

Applicant: CRITITECH, INC.

Inventor： Michael BALTEZOR ,  Joseph FARTHING ,  Jake SITTENAUER ,  Jahna ESPINOSA ,  Samuel CAMPBELL ,  Matthew MCCLOREY ,  Julia K. FISCHER ,  Mark D. WILLIAMS ,  Gary CLAPP

IPC: A61K31/337 ,  B01J3/02 ,  A61K9/16 ,  B01J3/00

CPC classification number: A61K31/337 ,  A61J3/02 ,  A61K9/0019 ,  A61K9/10 ,  A61K9/14 ,  A61K9/1605 ,  A61K9/1682 ,  A61K9/1688 ,  A61K9/5192 ,  B01D46/24 ,  B01D2271/02 ,  B01J2/04 ,  B01J3/008 ,  B01J3/02 ,  B01J4/002 ,  B01J19/10 ,  B01J19/26 ,  B05B1/3489 ,  B05B13/0278 ,  B05D2401/90

Abstract: Compositions are provided that include having at least 95% by weight of a taxane, or a pharmaceutically acceptable salt thereof, where the particles have a mean bulk density between about 0.050 g/cm3 and about 0.15 g/cm3, and/or a specific surface area (SSA) of at least 18 m2/g, 20 m2/g, 25 m2/g, 30 m2/g, 32 m2/g, 34 m2/g, or 35 m2/g. Methods for making and using such compositions are also provided.

公开(公告)号：US09918957B2

公开(公告)日：2018-03-20

申请号：US15499397

申请日：2017-04-27

Applicant: CRITITECH, INC.

Inventor： Michael Baltezor ,  Joseph Farthing ,  Jake Sittenauer ,  Jahna Espinosa ,  Samuel Campbell ,  Matthew McClorey ,  Julia K. Fischer ,  Mark D. Williams

IPC: A61K31/337 ,  A61K9/16 ,  B01J3/02 ,  B01J3/00

CPC classification number: A61K31/337 ,  A61J3/02 ,  A61K9/0019 ,  A61K9/10 ,  A61K9/14 ,  A61K9/1605 ,  A61K9/1682 ,  A61K9/1688 ,  A61K9/5192 ,  B01D46/24 ,  B01D2271/02 ,  B01J2/04 ,  B01J3/008 ,  B01J3/02 ,  B01J4/002 ,  B01J19/10 ,  B01J19/26 ,  B05B1/3489 ,  B05B13/0278 ,  B05D2401/90

Abstract: Compositions are provided that include having at least 95% by weight of a taxane, or a pharmaceutically acceptable salt thereof, where the particles have a mean bulk density between about 0.050 g/cm3 and about 0.15 g/cm3, and/or a specific surface area (SSA) of at least 18 m2/g, 20 m2/g, 25 m2/g, 30 m2/g, 32 m2/g, 34 m2/g, or 35 m2/g. Methods for making and using such compositions are also provided.

公开(公告)号：US20180043279A1

公开(公告)日：2018-02-15

申请号：US15469990

申请日：2017-03-27

Applicant: George L. Quinlan

Inventor： George L. Quinlan

IPC: B01D3/40 ,  B01D3/36

CPC classification number: B01D3/40 ,  B01D3/14 ,  B01D3/16 ,  B01D3/26 ,  B01D3/30 ,  B01D3/36 ,  B01D11/0203 ,  B01D11/0403 ,  B01D11/0407 ,  B01J3/008 ,  C07C45/82 ,  C07C49/395 ,  H01L21/02101

Abstract: Certain embodiments described herein are directed to separation systems and methods effective to separate two or more solvents in a solvent mixture. In certain examples, a system effective to separate two or more azeotrope forming solvents is provided. In some embodiments, the system can be effective to remove at least about 95% of one of the solvents from the solvent mixture.

公开(公告)号：US09843035B2

公开(公告)日：2017-12-12

申请号：US14438300

申请日：2013-11-27

Applicant: LG Chem, Ltd.

Inventor： Hyun Kuk Noh ,  Hong Kyu Park ,  Chi Ho Jo ,  Ji Hoon Ryu ,  Sang Seung Oh ,  Wang Mo Jung

IPC: B01J19/02 ,  B01J19/24 ,  H01M4/136 ,  B01J19/18 ,  H01M4/58 ,  B01J3/00 ,  B01J3/02 ,  B01J4/00 ,  H01M4/02

CPC classification number: H01M4/136 ,  B01J3/008 ,  B01J3/02 ,  B01J4/002 ,  B01J19/02 ,  B01J19/18 ,  B01J19/24 ,  B01J2204/007 ,  B01J2219/00094 ,  B01J2219/00247 ,  B01J2219/00252 ,  B01J2219/0204 ,  B01J2219/0209 ,  B01J2219/0236 ,  B01J2219/0245 ,  B01J2219/0286 ,  H01M4/5825 ,  H01M2004/028 ,  Y02P20/544

Abstract: Disclosed is a hydrothermal synthesis device for continuously preparing an inorganic slurry using a hydrothermal method. The hydrothermal synthesis device includes a mixer to mix at least one precursor solution for preparing an inorganic material, injected via at least one supply tube, to prepare an intermediate slurry, a connection tube provided at a side of the mixer, continuously discharging the prepared intermediate slurry to a reactor, and having a hydrophobic coating on an inner surface of a portion thereof adjacent to the reactor, and the reactor performing hydrothermal reaction of the intermediate slurry supplied from the connection tube by receiving a liquid stream heated to supercritical or subcritical conditions using a heat exchanger and connected to the connection tube into which the intermediate slurry prepared from the mixer is introduced and to at least one injection tube into which the heated liquid stream is injected.

公开(公告)号：US20170266613A1

公开(公告)日：2017-09-21

申请号：US15611755

申请日：2017-06-01

Applicant: XI'AN JIAOTONG UNIVERSITY

Inventor： Shuzhong Wang ,  Mengmeng Ren ,  Xingying Tang ,  Jie Zhang ,  Yuzhen Wang ,  Yanhui Li

IPC: B01D53/78 ,  B01J19/24

CPC classification number: B01J3/008 ,  B01J2219/00054 ,  B01J2219/00103 ,  Y02P20/544

Abstract: An intermediate medium heat exchanging device for a supercritical water oxidation system includes a material main loop, an intermediate medium loop and a replenishment branch. A material pump, a preheater, a spray type desuperheater, a reactor and a regenerator are connected in sequence to form the material main loop; a buffer tank, a circulating pump, the regenerator, the preheater and a water cooler form the intermediate medium loop. A back pressure valve is located above the buffer tank. The replenishment branch includes a cooling water pump, an outlet of the cooling water pump is divided into two sub-branches, one sub-branch is connected with the spray type desuperheater, and another sub-branch is connected with the buffer tank. The intermediate medium heat exchanging device is reasonable in structural design, and is able to maximally reduce the investment cost and ensure the stable operation of the system.

公开(公告)号：US09738943B2

公开(公告)日：2017-08-22

申请号：US13882868

申请日：2011-10-28

Applicant: Andreas Gram ,  Haukur Johannesson

Inventor： Rune Ekman ,  Andreas Gram ,  Haukur Johannesson

IPC: C13K1/02 ,  B01J3/00 ,  C13K13/00 ,  C08B1/00 ,  C08H8/00 ,  C12P7/10 ,  C13K11/00 ,  D21B1/02

CPC classification number: C13K1/02 ,  B01J3/008 ,  B01J2219/00029 ,  B01J2219/00036 ,  B01J2219/00177 ,  C08B1/003 ,  C08H8/00 ,  C12P7/10 ,  C12P2201/00 ,  C13K11/00 ,  C13K13/00 ,  C13K13/007 ,  D21B1/021 ,  Y02E50/16 ,  Y02P20/544

Abstract: The present invention describes a process for a controlled conversion of a biomass feedstock, wherein the process comprises the steps of: loading the biomass feedstock to at least one reactor; liquefaction of the biomass feedstock into a monomer and/or oligomer sugar mixture in said reactor by treatment in hot compressed liquid water (HCW) at sub- and/or super-critical condition; and removal of the monomer and/or oligomer sugar mixture, being the product molecules, to avoid continued detrimental decomposition.

公开(公告)号：US09670419B2

公开(公告)日：2017-06-06

申请号：US15397116

申请日：2017-01-03

Applicant: Saudi Arabian Oil Company

Inventor： Ki-Hyouk Choi ,  Joo-Hyeong Lee ,  Abdullah T. Alabdulhadi

IPC: B01J19/24 ,  C10G9/40

CPC classification number: C10G9/40 ,  B01D2253/102 ,  B01D2257/7025 ,  B01D2259/4525 ,  B01J3/008 ,  B01J19/2415 ,  B01J20/20 ,  B01J20/28045 ,  B01J20/28066 ,  B01J20/28073 ,  B01J20/28076 ,  B01J20/3057 ,  B01J20/3078 ,  B01J20/3204 ,  B01J20/3214 ,  B01J2219/00094 ,  B01J2219/00105 ,  B01J2219/0011 ,  B01J2219/00135 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/24 ,  C01B32/05 ,  C01B32/306 ,  C10G1/002 ,  C10G1/065 ,  C10G31/08 ,  C10G45/26 ,  C10G49/18 ,  C10G55/04 ,  C10G2300/202 ,  C10G2300/206 ,  C10G2300/708

Abstract: A process for reducing coke formation during hydrocarbon upgrading reactions using a double-wall reactor comprising the steps of feeding a heated feed water to a shell-side volume of the double-wall reactor to produce a heat transfer stream, the double-wall reactor comprising an exterior wall and an interior wall, a reaction section volume, a heating element configured to heat the heat transfer stream, wherein heat is transferred from the heat transfer stream to the reaction section volume, feeding the hot water return exiting the shell-side volume through a filter; mixing the filtered water stream with a heated hydrocarbon feedstock; feeding the mixed stream to the reaction section volume in a configuration counter-current to the heat transfer stream; reacting the reaction flow stream at a reaction temperature, wherein the heat transferred to the reaction section volume is operable to maintain the reaction temperature above the critical temperature of water.

公开(公告)号：US09604194B2

公开(公告)日：2017-03-28

申请号：US14513707

申请日：2014-10-14

Applicant: Saudi Arabian Oil Company ,  Korea Advanced Institute of Science and Technology

Inventor： Yuguo Wang ,  Cemal Ercan ,  Rashid M. Othman ,  Minkee Choi ,  Seokin Choi

IPC: C01B31/02 ,  B01J20/20 ,  B01J20/28 ,  B01J20/32 ,  B01J20/30 ,  C01B31/08 ,  B01J19/24 ,  B01J3/00 ,  C10G31/08 ,  C10G45/26 ,  C10G49/18 ,  C10G1/06

CPC classification number: B01J20/20 ,  B01D2253/102 ,  B01D2257/7025 ,  B01D2259/4525 ,  B01J3/008 ,  B01J19/2415 ,  B01J20/28045 ,  B01J20/28066 ,  B01J20/28073 ,  B01J20/28076 ,  B01J20/3057 ,  B01J20/3078 ,  B01J20/3204 ,  B01J20/3214 ,  B01J2219/00094 ,  B01J2219/00105 ,  B01J2219/0011 ,  B01J2219/00135 ,  B01J2219/00157 ,  B01J2219/00159 ,  C01B32/05 ,  C01B32/306 ,  Y02C20/20 ,  Y02P20/134

Abstract: A methane microporous carbon adsorbent comprising a thermally-treated CVD carbon having a shape in the form of a negative replica of a crystalline zeolite has a BET specific surface area, a micropore volume, a micropore to mesopore volume ratio, a stored methane value and a methane delivered value and a sequential carbon synthesis method for forming the methane microporous carbon adsorbent. Introducing an organic precursor gas for a chemical vapor deposition (CVD) period to a crystalline zeolite that is maintained at a CVD temperature forms the carbon-zeolite composite. Introducing a non-reactive gas for a thermal treatment period to the carbon-zeolite composite maintained at a thermal treatment temperature forms the thermally-treated carbon-zeolite composite. Introducing an aqueous strong mineral acid mixture to the thermally-treated carbon-zeolite composite forms the methane microporous carbon adsorbent.

公开(公告)号：US20170021427A1

公开(公告)日：2017-01-26

申请号：US15301388

申请日：2014-11-10

Applicant: XI'AN JIAOTONG-UNIVERSITY ,  XI'AN WONFU ENERGY AND ENVIROMENT TECHNOLOGIES CO., LTD.

Inventor： Shuzhong Wang ,  Lu Zhou ,  Yanmeng Gong ,  Lili Qian ,  Mengmeng Ren ,  Yanhui LI

IPC: B22F9/24 ,  F27D99/00 ,  B01D19/00 ,  B01J3/04 ,  B01D17/02 ,  B01D36/00 ,  B01J3/00 ,  B22F1/00 ,  B01D21/26

CPC classification number: B22F9/24 ,  B01D17/02 ,  B01D17/0217 ,  B01D19/0068 ,  B01D21/26 ,  B01D21/262 ,  B01D36/008 ,  B01J3/008 ,  B01J3/04 ,  B22F1/0018 ,  B22F2201/05 ,  B22F2202/03 ,  B22F2998/10 ,  F27D99/0001 ,  F27D2099/0058

Abstract: A system for preparing nanoparticles by supercritical hydrothermal synthesis is provided. Firstly, a mixture of a first reactant and a second reactant and high-temperature water at an outlet of a heating furnace (10) are mixed and are heated to a reaction temperature, the mixture is connected to a supercritical hydrothermal synthesis reactor (14), and a product at an outlet of the supercritical hydrothermal synthesis reactor enters a heat regenerator (9); hot water at an outlet of a low-temperature section of the heating furnace (10) first enters the heat regenerator, and then enters a high-temperature section of the heating furnace so as to be continuously heated to a set temperature; fluid at the pipe side outlet of the heat regenerator separately passes through a heat exchange coil in a first reactant modulation pool (1) and a steam generator (2) in a waste heat power generation system (20).

Abstract translation: 提供了一种通过超临界水热合成制备纳米颗粒的系统。 首先，在加热炉（10）的出口处混合第一反应物和第二反应物和高温水，并加热至反应温度，将混合物连接到超临界水热合成反应器（14） 并且超临界水热合成反应器出口处的产物进入热再生器（9）; 在加热炉（10）的低温部的出口处的热水首先进入蓄热体，然后进入加热炉的高温部分，以连续加热至设定温度; 在再生器的管侧出口处的流体分别通过废热发电系统（20）中的第一反应物调制池（1）和蒸汽发生器（2）中的热交换盘管。

公开(公告)号：US20170015578A1

公开(公告)日：2017-01-19

申请号：US15124558

申请日：2015-03-10

Applicant: INNOVEOX

Inventor： Grégoire Sarrail ,  Carine Richer ,  Mathieu Chaillou

IPC: C02F11/08 ,  B01J3/00 ,  B01F17/00 ,  C02F1/72 ,  C02F1/74

CPC classification number: C02F11/086 ,  B01F17/0021 ,  B01F17/0028 ,  B01F17/0078 ,  B01F17/0085 ,  B01J3/006 ,  B01J3/008 ,  C02F1/727 ,  C02F1/74 ,  C02F2101/32 ,  C02F2209/001 ,  C02F2209/08 ,  C02F2209/20 ,  C02F2209/225 ,  C02F2305/04

Abstract: The present invention relates to a method for treating waste comprising at least one organic phase, said method comprising the following consecutive steps: a) preparation of an oil-in-water emulsion with controlled TOD using waste to be treated comprising at least one organic phase, by mixing said waste with an aqueous phase in a mixer, preferably with high shear; b) possible adjustment of the TOD of the emulsion obtained in step a); and c) hydrothermal oxidation, under subcritical or supercritical starting conditions, of the emulsion thus obtained. The present invention also relates to a facility suitable for implementing the method for treating waste comprising at least one organic phase according to the invention.

Abstract translation: 本发明涉及一种用于处理包含至少一种有机相的废物的方法，所述方法包括以下连续步骤：a）使用待处理的废物制备具有受控TOD的水包油乳液，其包含至少一种有机相 通过将混合物中的所述废物与水相混合，优选在高剪切下混合; b）可能调节在步骤a）中获得的乳液的TOD; 和c）在亚临界或超临界起始条件下由如此获得的乳液进行水热氧化。 本发明还涉及适用于实施根据本发明的至少一种有机相处理废物的方法的设备。