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公开(公告)号:US12187667B2
公开(公告)日:2025-01-07
申请号:US18657754
申请日:2024-05-07
Applicant: ZHEJIANG HUAKANG PHARMACEUTICAL CO., LTD.
Inventor: Qiang Wu , Mian Li , Wenyao Zhang , Wulong Yang , Weidong Xu , Shufang Qin , Ni Zhen
Abstract: Disclosed is a preparation system and a preparation method for high-quality xylitol crystals. The preparation system comprises a blending tank, a heat exchanger, a decolorization tank, an ion exchange system, a microporous filter, a first evaporator, a first crystallization kettle, a first centrifuge, a fluidization drying bed, a xylitol dissolution tank, a second evaporator, a second crystallization kettle, a second centrifuge, a hot air drying tank, and a cold air fluidization bed sequentially connected through pipelines. Liquid outlet of the first centrifuge is connected with first inlet of the blending tank. Liquid outlet of the second centrifuge is connected with first inlet of the xylitol dissolution tank. The blending tank is provided with second inlet for receiving xylitol hydrogenation solution. The xylitol dissolution tank is provided with water inlet for pure water. The material output from a product outlet of the cold air fluidization bed is xylitol crystal product. First prepared xylitol crystals are redissolved and recrystallized to prepare xylitol crystals with higher pH and better flavor.
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公开(公告)号:US20240300877A1
公开(公告)日:2024-09-12
申请号:US18661567
申请日:2024-05-10
Applicant: ZHEJIANG HUAKANG PHARMACEUTICAL CO., LTD.
Inventor: Mian LI , Weidong XU , Deshui CHEN , Xinping CHENG , Chengjun LIAO , Qiang WU , Wulong YANG , Shufang QIN
IPC: C07C29/88 , C07C29/141 , C07C29/78 , C07C29/90 , C09B67/20
CPC classification number: C07C29/88 , C07C29/141 , C07C29/78 , C07C29/90 , C09B67/006 , B01D2311/04
Abstract: The present disclosure provides a method for co-producing a xylitol and a caramel pigment. The method includes: transporting a raw material of a xylose mother liquid in a raw material tank to a filter for filtering impurities to obtain a filtered raw material of the xylose mother liquid, and transporting the filtered raw material of the xylose mother liquid to a nanofiltration membrane device to obtain a decolorized xylose mother liquid; transporting the decolorized xylose mother liquid to a first ion exchange device to obtain an ion exchange liquid; and transporting the ion exchange liquid to a chromatographic separation device and obtaining an extracted liquid and a raffinate liquid; performing a refined hydrogenation process on the extracted liquid through a refined hydrogenation assembly to obtain a crystal xylitol, and performing a browning reaction process on the raffinate liquid through a browning reaction assembly to obtain the caramel pigment.
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公开(公告)号:US11970436B2
公开(公告)日:2024-04-30
申请号:US17749293
申请日:2022-05-20
Applicant: NEONC Technologies, Inc.
Inventor: Thomas Chen , Daniel Levin , Satish Puppali
IPC: C07C29/92 , A61K31/045 , A61K31/4188 , A61K45/06 , A61N5/10 , C07C29/78 , C07C29/86 , C07C29/88 , C07C67/14 , C07C201/12 , C07C201/16
CPC classification number: C07C29/92 , A61K31/045 , A61K31/4188 , A61K45/06 , A61N5/10 , C07C29/78 , C07C29/86 , C07C29/88 , C07C67/14 , C07C201/12 , C07C201/16 , C07B2200/07 , C07C2601/16 , C07C29/92 , C07C33/14 , C07C201/12 , C07C205/57 , C07C67/14 , C07C69/76 , C07C67/14 , C07C69/92
Abstract: The present invention provides a process for purifying a monoterpene or sesquiterpene having a purity greater than about 98.5% (w/w). The process comprises the steps of derivatizing the monoterpene (or sesquiterpene) to produce a monoterpene (or sesquiterpene) derivative, separating the monoterpene (or sesquiterpene) derivative, and releasing the monoterpene (or sesquiterpene) from the derivative. Also encompassed by the scope of the present invention is a pharmaceutical composition comprising a monoterpene (or sesquiterpene) having a purity greater than about 98.5% (w/w). The purified monoterpene can be used to treat a disease such as cancer. The present monoterpene (or sesquiterpene) may be administered alone, or may be co-administered with radiation or other therapeutic agents, such as chemotherapeutic agents.
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公开(公告)号:US11939284B2
公开(公告)日:2024-03-26
申请号:US18328581
申请日:2023-06-02
Applicant: Twelve Benefit Corporation
Inventor: Luka Stevic
IPC: C07C51/12 , C07C29/151 , C07C29/78 , C07C51/43
CPC classification number: C07C51/12 , C07C29/1518 , C07C29/78 , C07C51/43
Abstract: Systems and methods for acetic acid production include synthesizing acetic acid from carbon monoxide produced by a carbon dioxide electrolyzer and hydrogen produced by a water electrolyzer.
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公开(公告)号:US20240051909A1
公开(公告)日:2024-02-15
申请号:US18328581
申请日:2023-06-02
Applicant: Twelve Benefit Corporation
Inventor: Luka Stevic
IPC: C07C51/12 , C07C29/151 , C07C29/78 , C07C51/43
CPC classification number: C07C51/12 , C07C29/1518 , C07C29/78 , C07C51/43
Abstract: Systems and methods for acetic acid production include synthesizing acetic acid from carbon monoxide produced by a carbon dioxide electrolyzer and hydrogen produced by a water electrolyzer.
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公开(公告)号:US11840501B2
公开(公告)日:2023-12-12
申请号:US17288020
申请日:2020-03-13
Applicant: Zhejiang Huakang Pharmaceutical Co., Ltd. , Zhejiang University , Zhejiang University of Technology
Inventor: Jian Yang , Yi Zheng , Taogang Zhang , Han Gao , Mian Li , Zhiqiang Liu , Yuguo Zheng , Baoxing Mao , Xiaojian Zhang , Weiwei Fan
CPC classification number: C07C29/78 , A23L27/34 , B01D1/26 , B01D9/0022 , B01D21/262 , C07C31/18 , A23V2002/00 , B01D2009/0086
Abstract: The present invention relates to a xylitol preparation device integrating evaporation, crystallization and centrifugation, including a xylitol tank, a cleaning liquid tank, a recycling tank and a multiple distribution system, wherein the multiple distribution system includes J groups of evaporators for evaporation concentration, K groups of vacuum crystallization kettles for vacuum crystallization and L groups of centrifuges for centrifugation, wherein 2≤J≤6, 6≤K≤12 and 2≤L≤4; the evaporator, the vacuum crystallization kettle and the centrifuge in different groups are sequentially connected in series with one another through a pipeline and a valve respectively; by controlling on and off of each valve, a xylitol exchange liquid is switched and controlled between a series-connection mode and a parallel-connection mode in the multiple distribution system to enable evaporation, crystallization and separation processes to reach an optimal effect distribution so as to improve productivity. The present invention further discloses a control method of the device. The processes and equipment of the present invention are highly integrated to realize continuous integrated production of xylitol preparation with low energy consumption and high automation degree, and full utilization of raw materials.
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公开(公告)号:US20230058914A1
公开(公告)日:2023-02-23
申请号:US17796197
申请日:2021-02-01
Applicant: Topsoe A/S
Inventor: Emil Andreas Tjärnehov
IPC: C07C29/152 , C07C29/78 , B01J19/24
Abstract: Process and reaction system for the preparation of methanol. The process comprises the steps of (a) providing a fresh methanol synthesis gas containing hydrogen, carbon monoxide and carbon dioxide; (b)) introducing and reacting the fresh methanol synthesis gas stream in a first methanol reaction unit in presence of a methanol catalyst and obtaining a first effluent stream containing methanol and unconverted synthesis gas; (c) providing a recycle gas stream containing the unconverted methanol synthesis gas contained in the first effluent stream and unconverted methanol synthesis gas from a second methanol reaction unit; (d) introducing and reacting the recycle gas stream in the second methanol reaction unit in presence of a methanol catalyst; (e) withdrawing a second effluent stream containing methanol and the unconverted methanol synthesis gas from the second methanol reaction unit; (f)) combining the first and a part of the second effluent stream; (g) cooling and separating the combined effluent into a methanol-containing liquid stream and the recycle stream; and (h) withdrawing the remaining part of the second effluent stream a purge gas stream,wherein the remaining part of he second effluent stream is withdrawn as a purge gas stream prior to combining the first and second effluent stream.
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公开(公告)号:US11325877B2
公开(公告)日:2022-05-10
申请号:US16765647
申请日:2018-11-20
Applicant: SHELL OIL COMPANY
Inventor: Ram Paul Bajaj , Peter Molenaar
Abstract: A process for the recovery of ethylene glycol from an aqueous stream comprising ethylene glycol is disclosed. The process comprises (a) subjecting an aqueous stream 5 comprising ethylene glycol to an evaporation step in a multiple-effect evaporator to obtain a concentrated stream comprising ethylene glycol; (b) subjecting said concentrated stream comprising ethylene glycol to a first dehydration step in a first dehydrator 10 operating at an overhead pressure in the range of 0 barg (bar gauge) to 4 barg (bar gauge) to obtain a partially dehydrated ethylene glycol stream, and (c) subjecting said partially dehydrated ethylene glycol stream to a second dehydration step in a second dehydrator operating under 15 vacuum to obtain a dehydrated ethylene glycol stream.
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公开(公告)号:US20210395174A1
公开(公告)日:2021-12-23
申请号:US17288020
申请日:2020-03-13
Applicant: Zhejiang Huakang Pharmaceutical Co., Ltd. , Zhejiang University , Zhejiang University of Technology
Inventor: Jian Yang , Yi ZHENG , Taogang ZHANG , Han GAO , Mian LI , Zhiqiang LIU , Yuguo ZHENG , Baoxing MAO , Xiaojian ZHANG , Weiwei FAN
Abstract: The present invention relates to a xylitol preparation device integrating evaporation, crystallization and centrifugation, including a xylitol tank, a cleaning liquid tank, a recycling tank and a multiple distribution system, wherein the multiple distribution system includes J groups of evaporators for evaporation concentration, K groups of vacuum crystallization kettles for vacuum crystallization and L groups of centrifuges for centrifugation, wherein 2≤J≤6, 6≤K≤12 and 2≤L≤4; the evaporator, the vacuum crystallization kettle and the centrifuge in different groups are sequentially connected in series with one another through a pipeline and a valve respectively; by controlling on and off of each valve, a xylitol exchange liquid is switched and controlled between a series-connection mode and a parallel-connection mode in the multiple distribution system to enable evaporation, crystallization and separation processes to reach an optimal effect distribution so as to improve productivity. The present invention further discloses a control method of the device. The processes and equipment of the present invention are highly integrated to realize continuous integrated production of xylitol preparation with low energy consumption and high automation degree, and full utilization of raw materials.
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公开(公告)号:US20210340086A1
公开(公告)日:2021-11-04
申请号:US17271597
申请日:2020-05-07
Applicant: SUZHOU SUZHEN BIOENGINEERING CO., LTD
Inventor: Ji An LUO , Guozhu SHI , Yun ZHANG , Bin LIU , Juanjuan QIAN , Juan DING , Wei WANG , Wei JI
Abstract: A method for extracting polyol from a fermentation process is disclosed. The preparing method includes rectifying and purifying PDO (1,3-propanediol) from a polyol fermentation broth after concentration to form a steam condensate, wherein the concentration is a evaporative dehydration; and filtering the steam condensate through a reverse osmosis membrane to form a concentrated solution, wherein the retentate of the reverse osmosis flows back to the evaporative dehydration, and the penetrant of the reverse osmosis can be reused as a fermentation ingredient, as cleaning water or for sewage treatment; and the water content of the concentrated solution after the evaporative dehydration is 5-25 wt %; and the yield of PDO is ≥99.5%. The preparing method meets the requirements of water resources recycling, reduces the production loss of PDO and BDO (2,3-butanediol) during the concentration, and greatly cuts down on the amount of wastewater.
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