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公开(公告)号:US12209804B2
公开(公告)日:2025-01-28
申请号:US17631531
申请日:2020-08-24
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Nasser Mansour Alsubaie , Ahmed Abouelfetouh Youssef , Allen Lee White , Vern Lowry
Abstract: A rotary dryer for resin dehydration, comprising: a cylindrical body which rotates about an axis perpendicular to a diameter of the cylindrical body; an air filter located outside the cylindrical body; coils located outside the cylindrical body, wherein the coils are oriented vertically and oriented parallel to the diameter of the cylindrical body, wherein the coils do not comprise horizontal surfaces; and lifters located within the cylindrical body.
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公开(公告)号:US20220370969A1
公开(公告)日:2022-11-24
申请号:US17879941
申请日:2022-08-03
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Dane M. Ferraris , Richard Legg , Ahmed Abouelfetouh Youssef , Vern Lowry
IPC: B01F25/451 , F04B15/02 , F04B53/08 , F04B53/18 , F04B53/16
Abstract: The invention relates to a piston system (1) for use in a homogenizer, comprising a piston (2) that is configured and arranged to make a reciprocating movement in use of the piston system, a cylinder (3) that is configured and arranged to receive and guide at least a first part of the piston, a first supply channel (8) that is configured and arranged to supply a lubricating medium (9) to a portion (10) of the first part of the piston that in use is arranged inside the cylinder, and a second supply channel (13) that is configured and arranged to, in use, supply a cooling medium (14) to a second part of the piston outside the cylinder. Also disclosed is a process for the production of an elastomer agglomerate composition forcing a slurry comprising elastomeric particles through an aperture to obtain the elastomer agglomerate composition using the piston system.
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公开(公告)号:US20200061869A1
公开(公告)日:2020-02-27
申请号:US16466507
申请日:2017-12-06
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Ahmed Abouelfetouh Youssef , Vern Lowry , Dane Ferraris , Jianhua Xu
Abstract: A process for the production of an elastomer agglomerate composition wherein the process comprises the steps in this order: (a) providing a slurry comprising elastomeric particles having an average particle size of ≤150 nm in water; and (b) forcing the slurry from (a) through an aperture at a flow velocity of at least 500 m/s. The elastomer agglomerate compositions produced via such process demonstrate a particularly desirable high average particle size.
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14.
公开(公告)号:US10407370B2
公开(公告)日:2019-09-10
申请号:US15751190
申请日:2016-08-09
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Mark Erik Nelson , Ahmed Abouelfetouh Youssef , Karl Aaron Baro , Paulus Johannes Maria Eijsbouts
Abstract: In an embodiment, a method of recovering phenol from a bisphenol A production facility comprises reacting phenol and acetone to produce a bisphenol A stream; separating the bisphenol A stream into a product bisphenol A stream and a purge stream; separating the purge stream into a primary top outlet stream and a primary bottom outlet stream; adding an acid catalyst to the primary bottom outlet stream to form a cracker inlet stream; separating the cracker inlet stream into a cracker top outlet stream and a cracker bottom outlet stream; separating the cracker top outlet stream and the cracker bottom outlet stream into a secondary top outlet stream and a secondary bottom outlet stream; forming a bisphenol A plant phenol recovery stream; combining the bisphenol A plant phenol recovery stream with a stream of a phenol purification plant.
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15.
公开(公告)号:US20190225717A1
公开(公告)日:2019-07-25
申请号:US16330314
申请日:2017-08-21
Applicant: SABIC Global Technologies B.V.
Inventor: Ahmed Abouelfetouh Youssef , Vern Lowry , Dane Ferraris
IPC: C08F6/00
Abstract: The present invention relates to a process for the production of a polymer using a compound comprising at least 2 unsaturated carbon-carbon bonds, wherein the process comprises a polymerisation section and a purification section, wherein the product from the polymerisation section is subjected in the purification section to a sequence of purification steps comprising: ⋅removal of the vapour phase from the product from the polymerisation section by means of flash separation to obtain a first vapour phase and a polymerisation product; ⋅subjecting the first vapour phase to a compression and condensation treatment to obtain a second vapour phase and a condensed monomer phase; wherein the purification steps are conducted in this order. Such process allows for the optimal utilisation of raw materials in the polymerisation process.
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16.
公开(公告)号:US10246391B2
公开(公告)日:2019-04-02
申请号:US15757070
申请日:2016-11-22
Applicant: Sabic Global Technologies B.V.
Inventor: Mark Erik Nelson , Ahmed Abouelfetouh Youssef
IPC: C07C37/00 , C07C37/08 , C07C37/20 , C07C37/68 , C07C37/74 , C07C37/80 , C07C37/84 , C07C39/04 , C07C39/16
Abstract: In an embodiment, a method of recovering an unreacted phenol from a bisphenol A production facility comprises reacting an initial phenol and an initial acetone in the presence of a catalyst to produce a bisphenol A stream comprising the unreacted phenol of the initial phenol and a bisphenol A, separating a purge stream comprising the unreacted phenol, and wherein the unreacted phenol is present in the purge stream in an amount of 60 to 90 wt %, based on the total weight of the purge stream; adding the purge stream to a phenol purification section of a phenol production facility; and forming a purified phenol outlet stream in the phenol purification section, wherein the purified phenol outlet stream comprises a total phenol concentration of greater than or equal to 99.5 wt % based on the total weight of the purified phenol outlet stream.
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公开(公告)号:US20170240496A1
公开(公告)日:2017-08-24
申请号:US15421793
申请日:2017-02-01
Applicant: SABIC Global Technologies B.V.
Inventor: Mark Erik Nelson , Ahmed Abouelfetouh Youssef
CPC classification number: C07C45/80 , B01D11/0488 , B01J19/24 , B01J2219/24 , C07C37/20 , C07C45/82 , C07C39/16 , C07C49/08
Abstract: In an embodiment, a method of recovering acetone comprises separating a bisphenol A stream into a bisphenol A product stream and an extraction stream comprising unreacted acetone; recovering the unreacted acetone in a recovery section of the bisphenol A production facility and forming a bisphenol A plant acetone recovery stream comprising methanol and a recovered acetone; introducing the bisphenol A plant acetone recovery stream to a phenol purification plant; and purifying the bisphenol A plant acetone recovery stream in the phenol purification plant to form an acetone product stream. The acetone product stream can comprise a reduced amount of methanol as compared to the bisphenol A plant acetone recovery stream.
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