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公开(公告)号:US10695755B2
公开(公告)日:2020-06-30
申请号:US15921956
申请日:2018-03-15
Applicant: EASTMAN CHEMICAL COMPANY
Inventor: Mesfin Ejerssa Janka , Kenny Randolph Parker , Ashfaq Shahanawaz Shaikh , Lee Reynolds Partin
IPC: B01J27/32 , B01D11/04 , B01J27/128 , C07D307/68 , C07B41/08 , C07B63/00 , C07D307/48 , B01D17/00 , B01J10/00 , B01J23/889 , B01J38/12 , B01J35/12 , B01D3/06 , B01D3/14
Abstract: Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing various purification methods on the crude carboxylic acid.
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公开(公告)号:US09458122B2
公开(公告)日:2016-10-04
申请号:US14841867
申请日:2015-09-01
Applicant: Eastman Chemical Company
Inventor: Ashfaq Shahanawaz Shaikh , Kenny Randolph Parker , Mesfin Ejerssa Janka , Lee Reynolds Partin
IPC: C07D307/68
CPC classification number: C07D307/68
Abstract: A process to produce a dry purified furan-2,5-dicarboxylic acid (FDCA) is described. After oxidation of 5-(hydroxymethyl)furfural (5-HMF), a crude FDCA stream is produced that is fed to a crystallization zone followed by a solid-liquid displacement zone to form a low impurity slurry stream. The solids in the low impurity slurry stream are dissolved in a dissolution zone to produce a hydrogenation feed that is hydrogenated in a hydrogenation reactor to generate a hydrogenated FDCA composition. The hydrogenated FDCA composition is routed to a crystallization zone to form a crystallized produce stream that is separated from liquid in a solid-liquid separation zone to generate a purified wet cake stream containing FDCA that can be dried in a drying zone to generate a dry purified FDCA product stream.
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公开(公告)号:US20150087859A1
公开(公告)日:2015-03-26
申请号:US14034617
申请日:2013-09-24
Applicant: Eastman Chemical Company
Inventor: David Milton Lange , Ashfaq Shahanawaz Shaikh , Patrice L. Riesenberg , Mesfin Ejerssa Janka
IPC: C07C51/265
CPC classification number: C07C51/265 , C07C63/26
Abstract: Processes for producing terephthalic acid are disclosed, the processes including a step of combining in a reaction medium para-xylene, a solvent comprising water and a saturated organic acid having from 2-4 carbon atoms, and an oxygen-containing gas, at a temperature for example from about 145° C. to about 175° C., in the presence of a catalyst composition comprising cobalt, manganese, zirconium, and bromine, wherein the zirconium is present in the reaction medium in an amount, for example, from 1 ppm to 50 ppm with respect to the weight of the liquid in the reaction medium.
Abstract translation: 公开了制备对苯二甲酸的方法,该方法包括在反应介质中将对二甲苯,包含水和含有2-4个碳原子的饱和有机酸的溶剂和含氧气体在一定温度下混合的步骤 例如约145℃至约175℃,在包含钴,锰,锆和溴的催化剂组合物存在下,其中锆以例如1的量存在于反应介质中 相对于反应介质中液体的重量为ppm至50ppm。
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14.
公开(公告)号:US08969404B2
公开(公告)日:2015-03-03
申请号:US13758080
申请日:2013-02-04
Applicant: Eastman Chemical Company
Inventor: Mesfin Ejerssa Janka , Charles Edwan Sumner, Jr. , Shane Kipley Kirk , Ashfaq Shahanawaz Shaikh , Kenny Randolph Parker
IPC: A61K31/341 , C07D307/34 , C07D307/68
CPC classification number: C07D307/68
Abstract: A process for purifying a crude furan 2,5-dicarboxylic acid composition (cFDCA) by hydrogenation of a FDCA composition dissolved in a hydrogenation solvent such as water, and hydrogenating under mild conditions, such as at a temperature within a range of 130° C. to 225° C. by contacting the solvated FDCA composition with hydrogen in the presence of a hydrogenation catalyst under a hydrogen partial pressure within a range of 10 psi to 900 psi. A product FDCA composition is produced having a low amount of tetrahydrofuran dicarboxylic acid, a low b*, and a low amount of 5-formyl furan-2-carboxylic acid (FFCA).
Abstract translation: 通过氢化溶解在氢化溶剂如水中的FDCA组合物,并在温和条件下(例如在130℃的温度范围内)氢化来纯化粗呋喃2,5-二羧酸组合物(cFDCA)的方法 通过在10psi至900psi的氢分压下,在氢化催化剂存在下使溶剂化的FDCA组合物与氢气接触。 制备具有少量四氢呋喃二羧酸,低b *和少量5-甲酰基呋喃-2-羧酸(FFCA)的产品FDCA组合物。
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15.
公开(公告)号:US20140142326A1
公开(公告)日:2014-05-22
申请号:US13798235
申请日:2013-03-13
Applicant: EASTMAN CHEMICAL COMPANY
Inventor: Ashfaq Shahanawaz Shaikh , Kenny Randolph Parker , Mesfin Ejerssa Janka , Lee Reynolds Partin
IPC: C07D307/68 , F01K27/00
CPC classification number: C07D307/68 , F01K27/00
Abstract: Disclosed is a process for producing a dry, purified carboxylic acid product comprising furan-2,5-dicarboxylic acid (FDCA). Also disclosed is a method for treating an oxidation off-gas stream from such a process. The method features solvent as well as energy recovery from the off-gas stream.
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16.
公开(公告)号:US11655227B2
公开(公告)日:2023-05-23
申请号:US17301003
申请日:2021-03-22
Applicant: Eastman Chemical Company
Inventor: Kevin John Fontenot , Mesfin Ejerssa Janka , Kenny Randolph Parker , Ashfaq Shahanawaz Shaikh
IPC: C07D307/68 , B01D19/00 , B01D3/00 , B01D3/06 , B01D5/00 , B01D8/00 , C08G63/181 , C08G63/78 , C08G63/66 , C08G63/672
CPC classification number: C07D307/68 , B01D3/002 , B01D3/06 , B01D5/003 , B01D8/00 , B01D19/0036 , C08G63/181 , C08G63/66 , C08G63/672 , C08G63/78 , C08G63/785
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.
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公开(公告)号:US20220323880A1
公开(公告)日:2022-10-13
申请号:US17592276
申请日:2022-02-03
Applicant: Eastman Chemical Company , North Carolina State University
Inventor: Ashfaq Shahanawaz Shaikh , Thomas Allen Puckette , Scott Allen Owens , Syed Mohammed Maaz , Jack R. Edwards
Abstract: Selective recovery of C2 to C4 hydrocarbons is achieved through the use of a converging-diverging nozzle, or de Laval nozzle. The vapor stream comprising C2 to C4 hydrocarbons is fed into an inlet of a de Laval nozzle having a throat. The vapor stream may have an initial temperature of between 0° C. and 100° C., and an initial pressure of between 200 psig and 500 psig. In the de Laval nozzle, the vapor stream expands after passing through the throat of the de Laval nozzle, producing a vapor stream having reduced temperature and pressure. Then, C2 to C4 hydrocarbons condense from the reduced-temperature vapor stream as liquid droplets, which may be recovered. Fractionation of C2 to C4 hydrocarbons by means of a de Laval nozzle is possible; the technique allows selective recovery of propane from a mixture of propane and ethane.
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公开(公告)号:US20200324277A1
公开(公告)日:2020-10-15
申请号:US16914723
申请日:2020-06-29
Applicant: Eastman Chemical Company
Inventor: Mesfin Ejerssa Janka , Kenny Randolph Parker , Ashfaq Shahanawaz Shaikh , Lee Reynolds Partin
IPC: B01J27/32 , B01D11/04 , B01J27/128 , C07D307/68 , C07B41/08 , C07B63/00 , C07D307/48 , B01D17/00 , B01J10/00 , B01J23/889
Abstract: Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing various purification methods on the crude carboxylic acid.
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公开(公告)号:US09212121B2
公开(公告)日:2015-12-15
申请号:US14034617
申请日:2013-09-24
Applicant: Eastman Chemical Company
Inventor: David Milton Lange , Ashfaq Shahanawaz Shaikh , Patrice L. Riesenberg , Mesfin Ejerssa Janka
IPC: C07C51/265
CPC classification number: C07C51/265 , C07C63/26
Abstract: Processes for producing terephthalic acid are disclosed, the processes including a step of combining in a reaction medium para-xylene, a solvent comprising water and a saturated organic acid having from 2-4 carbon atoms, and an oxygen-containing gas, at a temperature for example from about 145° C. to about 175° C., in the presence of a catalyst composition comprising cobalt, manganese, zirconium, and bromine, wherein the zirconium is present in the reaction medium in an amount, for example, from 1 ppm to 50 ppm with respect to the weight of the liquid in the reaction medium.
Abstract translation: 公开了制备对苯二甲酸的方法,该方法包括在反应介质中将对二甲苯,包含水和含有2-4个碳原子的饱和有机酸的溶剂和含氧气体在一定温度下混合的步骤 例如约145℃至约175℃,在包含钴,锰,锆和溴的催化剂组合物存在下,其中锆以例如1的量存在于反应介质中 相对于反应介质中液体的重量为ppm至50ppm。
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20.
公开(公告)号:US08916720B2
公开(公告)日:2014-12-23
申请号:US13798257
申请日:2013-03-13
Applicant: Eastman Chemical Company
Inventor: Ashfaq Shahanawaz Shaikh , Kenny Randolph Parker , Mesfin Ejerssa Janka , Lee Reynolds Partin
IPC: C07D307/68 , F01K21/04
CPC classification number: F01K21/04 , C07D307/68 , F01K25/065
Abstract: Disclosed is a process for producing a dry, purified carboxylic acid product comprising furan-2,5-dicarboxylic acid (FDCA). Also disclosed is a method for treating an oxidation off-gas stream from such a process. The method features solvent as well as energy recovery from the off-gas stream.
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