公开(公告)号：US20190352242A1

公开(公告)日：2019-11-21

申请号：US16529287

申请日：2019-08-01

Applicant: Honeywell International Inc.

Inventor： Yuon Chiu ,  Stephen A. Cottrell ,  Gustavo Cerri ,  Jennifer W. McClaine ,  Tao Wang ,  Rajiv Ratna Singh ,  Rajiv Banavali

IPC: C07C17/386 ,  B01D3/14 ,  B01D3/36 ,  C07C19/01 ,  C07C21/18 ,  C07C17/38 ,  B01D3/00 ,  C01B7/19 ,  C07C17/383 ,  B01D3/06

Abstract: The present disclosure provides separation processes for removing heavy organics that are formed in various production processes of HCFO-1233zd(E). Such separation processes allow for the recovery and/or separation of the heavy organics from reactants that are used to form HCFO-1233zd(E), including HF. Such separation or recovery processes may utilize various separation techniques (e.g., decanting, liquid-liquid separation, distillation, and flash distillation) and may also utilize the unique properties of azeotropic or azeotrope-like compositions. Recovery of the heavy organic that is substantially free from HF may allow for their use in subsequent manufacture processes or disposal.

公开(公告)号：US10480354B2

公开(公告)日：2019-11-19

申请号：US15842205

申请日：2017-12-14

Applicant: Saudi Arabian Oil Company

Inventor： Mahmoud Bahy Mahmoud Noureldin ,  Akram Hamed Mohamed Kamel

IPC: F01K25/06 ,  B01D3/00 ,  B01D3/14 ,  B01D3/42 ,  C02F1/00 ,  C02F1/16 ,  C10L3/10 ,  F22B1/18 ,  F22B3/02 ,  F25J3/02 ,  B01D1/00 ,  B01D1/26 ,  B01D3/06 ,  C10G5/06 ,  C10G7/00 ,  C02F103/08 ,  F01K25/10 ,  F01K27/02

Abstract: Certain aspects of natural gas liquid fractionation plant waste heat conversion to simultaneous power and potable water using Kalina Cycle and modified multi-effect-distillation system can be implemented as a system. The system includes a waste heat recovery heat exchanger network coupled to multiple heat sources of a Natural Gas Liquid (NGL) fractionation plant. The heat exchanger network is configured to transfer at least a portion of heat generated at the multiple heat sources to a first buffer fluid and a second buffer fluid flowed through the first heat exchanger network. The system includes a first sub-system configured to generate power. The first sub-system is thermally coupled to the waste heat recovery heat exchanger. The system includes a second sub-system configured to generate potable water from brackish water. The second sub-system is thermally coupled to the waste heat recovery heat exchanger.

公开(公告)号：US10471387B2

公开(公告)日：2019-11-12

申请号：US15861163

申请日：2018-01-03

Applicant: Beijing Huashi United Energy Technology and Development Co., Ltd.

Inventor： Lin Li ,  Ke Lin ,  Gang Zhao ,  Lixin Guo

IPC: B01D53/52 ,  B01D53/80 ,  B01D53/96 ,  C01B17/05 ,  C10L3/10 ,  B01D1/00 ,  B01D1/16 ,  B01D1/28 ,  B01D3/06

Abstract: Provided is a renewable high efficient desulfurization process using a suspension bed, comprising mixing the desulfurization slurry with a hydrogen sulfide containing gas to obtain a first mixture, and passing the first mixture into a suspension bed reactor from bottom to top, with controlling the first mixture to have a dwell time of 5-60 minutes in the suspension bed reactor to allow they contact and react sufficiently with each other; and subjecting a second mixture obtained from the reaction to gas liquid separation to produce a rich solution and a purified gas, feeding the purified gas into a fixed bed reactor for carrying out a second desulfurization to obtain a second purified gas, subjecting the resulting rich solution to flash evaporation and then reacting with an oxygen-containing gas for carrying out regeneration. The process may reduce the sulfur content in the hydrogen sulfide containing gas from 2.4-140 g/Nm3 to 50 ppm or less by using a suspension bed, and further reduce the sulfur content to less than 10 ppm in conjunction with a fixed bed. The invention achieves high efficient desulfurization by combining the suspension bed with the fixed bed connected in series. The present invention has high regeneration efficiency, and the barren solution may be recycled for being used as the desulfurization slurry, without generating secondary pollution, which is very suitable for industrial promotion.

公开(公告)号：US10451359B2

公开(公告)日：2019-10-22

申请号：US15842515

申请日：2017-12-14

Applicant: Saudi Arabian Oil Company

Inventor： Mahmoud Bahy Mahmoud Noureldin ,  Akram Hamed Mohamed Kamel

IPC: F28D21/00 ,  C02F1/16 ,  F01K25/06 ,  F01K27/02 ,  B01D1/00 ,  B01D1/26 ,  C10G5/06 ,  C10G7/00 ,  B01D3/06 ,  B01D3/14 ,  F25J3/02 ,  B01D53/00 ,  B01D53/14 ,  B01D53/26 ,  C02F103/08 ,  F01K25/10

Abstract: Certain aspects of natural gas liquid fractionation plant waste heat conversion to power using Kalina Cycle can be implemented as a system. The system includes a waste heat recovery heat exchanger configured to heat a buffer fluid stream by exchange with a heat source in a natural gas liquid fractionation plant. The system includes a Kalina cycle energy conversion system, which includes one or more first energy conversion heat exchangers configured to heat a working fluid by exchange with the heated buffer fluid stream, a separator configured to receive the heated working fluid and to output a vapor stream of the working fluid and the liquid stream of the working fluid, and a turbine and a generator, wherein the turbine and generator are configured to generate power by expansion of the vapor stream of the working fluid.

公开(公告)号：US10436077B2

公开(公告)日：2019-10-08

申请号：US15842213

申请日：2017-12-14

Applicant: Saudi Arabian Oil Company

Inventor： Mahmoud Bahy Mahmoud Noureldin ,  Akram Hamed Mohamed Kamel

IPC: F01K27/02 ,  C02F1/16 ,  F25B27/02 ,  F28D21/00 ,  B01D1/00 ,  B01D1/26 ,  B01D3/06 ,  B01D3/14 ,  C10G5/06 ,  C10G7/00 ,  F25J3/02 ,  B01D53/00 ,  B01D53/14 ,  B01D53/26 ,  C02F103/08

Abstract: Certain aspects of a natural gas liquid fractionation plant waste heat conversion to potable water using modified multi-effect distillation system can be implemented as a system that includes a waste heat recovery heat exchanger network thermally coupled to multiple heat sources of a Natural Gas Liquid (NGL) fractionation plant. The heat exchanger network is configured to recover at least a portion of heat generated at the multiple heat sources. The system includes a sub-system thermally coupled to the waste heat recovery heat exchanger network to receive at least a portion of heat recovered by the heat exchanger network. The sub-system is configured to perform one or more operations using at least the portion of heat recovered by the heat exchanger network.

公开(公告)号：US10435488B2

公开(公告)日：2019-10-08

申请号：US15947943

申请日：2018-04-09

Applicant: Bryan M. Garner

Inventor： Bryan M. Garner

IPC: B01D3/06 ,  C08F6/12 ,  B01D50/00 ,  B01D46/00 ,  B01J8/00 ,  C08F6/00

Abstract: A method of processing a polymerization reactor effluent stream comprising utilizing a separation system that removes greater than 99% of the fine polymer particles in the polymerization reactor effluent, wherein the separation system is a bag filter system, and wherein the bag filter is designed and operated to minimize the time required for shutdowns and equipment cleaning.

公开(公告)号：US10421736B2

公开(公告)日：2019-09-24

申请号：US15925867

申请日：2018-03-20

Applicant: Eastman Chemical Company

Inventor： Kevin John Fontenot ,  Mesfin Ejerssa Janka ,  Kenny Randolph Parker ,  Ashfaq Shahanawaz Shaikh

IPC: C07D307/02 ,  C07D307/68 ,  B01D19/00 ,  B01D3/00 ,  C08G63/66 ,  C08G63/672 ,  C08G63/78 ,  B01D3/06 ,  B01D5/00 ,  B01D8/00 ,  C08G63/181

Abstract: Disclosed is a process to produce a purified vapor comprising dialkyl-furan-2,5-dicarboxylate (DAFD). Furan-2,5-dicarboxylic acid (FDCA) and an alcohol in an esterification zone to generate a crude diester stream containing dialkyl furan dicarboxylate (DAFD), unreacted alcohol, 5-(alkoxycarbonyl)furan-2-carboxylic acid (ACFC), and alkyl furan-2-carboxylate (AFC). The esterification zone comprises at least one reactor that has been previously used in an DMT process.

公开(公告)号：US10376859B2

公开(公告)日：2019-08-13

申请号：US15576214

申请日：2017-03-30

Applicant: STAMICARBON B.V.

Inventor： Juan Coloma González ,  Luc Louis Maria Dieltjens ,  Johannes Henricus Mennen

IPC: B01J19/00 ,  B01J19/18 ,  B01J19/24 ,  B01D3/06 ,  B01D3/14 ,  B01D5/00 ,  C07C273/04 ,  C07C275/02 ,  B01L3/06 ,  B01L3/14

Abstract: The invention is directed to a urea plant with a high pressure synthesis section and a recovery section. The high pressure synthesis section comprises a reactor, a stripper and a condenser, wherein the reactor operates at a higher pressure than the stripper and the condenser. The plant further includes a compression unit between the condenser and the reactor. The compression unit utilizes mechanical energy recovered from a decompression unit positioned downstream of the stripper and upstream of the recovery section.

公开(公告)号：US10358540B2

公开(公告)日：2019-07-23

申请号：US15618550

申请日：2017-06-09

Applicant: GM Global Technology Operations LLC

Inventor： Thomas J Chapaton ,  Wayne E Reeder

IPC: C08J11/02 ,  B01D3/14 ,  B01D1/00 ,  B01D3/06

Abstract: Volatile compound emissions from a product that comprises a polymeric material may be reduced or eliminated from the product by heating the product in a subatmospheric pressure environment. The product may be heated in the subatmospheric pressure environment at a temperature sufficient to vaporize a volatile compound contained within the polymeric material such that vapors of the volatile compound are extracted or released from the product.

公开(公告)号：US20190209943A1

公开(公告)日：2019-07-11

申请号：US16099375

申请日：2017-07-04

Applicant: I.D.E. TECHNOLOGIES LTD

Inventor： Tomer EFRAT ,  Alex DRAK

IPC: B01D1/26 ,  B01D9/00 ,  B01D3/06 ,  C02F1/06 ,  C02F1/04 ,  C02F1/68

Abstract: A thermal desalination system, comprising a multi-effect evaporator comprising a plurality of effects, configured to produce product water and brine and a fluidized bed crystallizer, configured to remove dissolved minerals and/or solids from the water, wherein the fluidized bed crystallizer is disposed between at least two effects of the multi-effect evaporator.