DE69217650T2 - Verfahren zum Entagglomerieren und Erneueren der Oberfläche eines Katalysators in einem Wirbelbett - Google Patents
Verfahren zum Entagglomerieren und Erneueren der Oberfläche eines Katalysators in einem WirbelbettInfo
- Publication number
- DE69217650T2 DE69217650T2 DE69217650T DE69217650T DE69217650T2 DE 69217650 T2 DE69217650 T2 DE 69217650T2 DE 69217650 T DE69217650 T DE 69217650T DE 69217650 T DE69217650 T DE 69217650T DE 69217650 T2 DE69217650 T2 DE 69217650T2
- Authority
- DE
- Germany
- Prior art keywords
- catalyst
- fluidized bed
- gas
- catalyst particles
- reactor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 128
- 238000000034 method Methods 0.000 title claims description 40
- 230000008569 process Effects 0.000 title claims description 32
- 239000002245 particle Substances 0.000 claims abstract description 43
- 238000005243 fluidization Methods 0.000 claims abstract description 11
- 239000000126 substance Substances 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 claims description 52
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 4
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 9
- 238000011109 contamination Methods 0.000 abstract description 3
- 238000005054 agglomeration Methods 0.000 abstract description 2
- 230000002776 aggregation Effects 0.000 abstract description 2
- 239000012530 fluid Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000356 contaminant Substances 0.000 description 5
- 239000007795 chemical reaction product Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/12—Treating with free oxygen-containing gas
- B01J38/30—Treating with free oxygen-containing gas in gaseous suspension, e.g. fluidised bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/31—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00654—Controlling the process by measures relating to the particulate material
- B01J2208/00681—Agglomeration
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S502/00—Catalyst, solid sorbent, or support therefor: product or process of making
- Y10S502/515—Specific contaminant removal
- Y10S502/518—Carbonaceous contaminant
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Catalysts (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/614,311 US5124291A (en) | 1990-11-15 | 1990-11-15 | Method for deagglomerating and re-exposing catalyst in a fluid bed reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| DE69217650D1 DE69217650D1 (de) | 1997-04-03 |
| DE69217650T2 true DE69217650T2 (de) | 1997-06-12 |
Family
ID=24460702
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE69217650T Expired - Fee Related DE69217650T2 (de) | 1990-11-15 | 1992-04-21 | Verfahren zum Entagglomerieren und Erneueren der Oberfläche eines Katalysators in einem Wirbelbett |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US5124291A (enExample) |
| EP (1) | EP0566785B1 (enExample) |
| CN (1) | CN1046639C (enExample) |
| AT (1) | ATE149099T1 (enExample) |
| DE (1) | DE69217650T2 (enExample) |
| ES (1) | ES2097870T3 (enExample) |
| TW (1) | TW204305B (enExample) |
Families Citing this family (37)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2156882A1 (en) * | 1994-09-06 | 1996-03-07 | Frederick John Kaiser Jr. | Process for selective catalyst particle size control by ex situ grinding to maintain bed fluidization during high temperature operations |
| US5421842A (en) * | 1994-09-06 | 1995-06-06 | Exxon Research And Engineering Company | High energy level in situ attrition and break up of catalyst to maintain bed fluidization during high temperature operations |
| US5877331A (en) * | 1997-11-12 | 1999-03-02 | Huntsman Petrochemical Corporation | Prevention of catalyst attrition and tar formation in manufacture of maleic anhydride |
| US9006175B2 (en) | 1999-06-29 | 2015-04-14 | Mannkind Corporation | Potentiation of glucose elimination |
| JP4416889B2 (ja) * | 1999-12-15 | 2010-02-17 | 株式会社日本触媒 | 固体触媒の廃棄方法 |
| EP1894591B1 (en) | 2002-03-20 | 2013-06-26 | MannKind Corporation | Cartridge for an inhalation apparatus |
| BRPI0514263B8 (pt) | 2004-08-20 | 2021-05-25 | Mannkind Corp | método para a síntese de bis-3,6-[4-aminobutil]-2,5-dicetopiperazina n-protegida |
| BR122019022692B1 (pt) | 2004-08-23 | 2023-01-10 | Mannkind Corporation | Composição terapêutica em pó seco contendo dicetopiperazina, pelo menos um tipo de cátion e um agente biologicamente ativo |
| CN101277764A (zh) | 2005-08-03 | 2008-10-01 | Ccmi公司 | 表面活性固相非均相催化剂的增强 |
| RU2394550C2 (ru) | 2005-09-14 | 2010-07-20 | Маннкайнд Корпорейшн | Способ получения лекарственной композиции, основанный на увеличении сродства поверхностей кристаллических микрочастиц к активным агентам |
| AU2007216966C1 (en) | 2006-02-22 | 2014-03-20 | Mannkind Corporation | A method for improving the pharmaceutic properties of microparticles comprising diketopiperazine and an active agent |
| US8485180B2 (en) | 2008-06-13 | 2013-07-16 | Mannkind Corporation | Dry powder drug delivery system |
| CN101827626B (zh) | 2008-06-13 | 2015-03-18 | 曼金德公司 | 干粉吸入器和用于药物输送的系统 |
| US9358352B2 (en) | 2008-06-13 | 2016-06-07 | Mannkind Corporation | Dry powder drug delivery system and methods |
| CA2728523C (en) | 2008-06-20 | 2020-03-10 | Mannkind Corporation | An interactive apparatus and method for real-time profiling of inhalation efforts |
| TWI494123B (zh) | 2008-08-11 | 2015-08-01 | Mannkind Corp | 超快起作用胰島素之用途 |
| US8314106B2 (en) | 2008-12-29 | 2012-11-20 | Mannkind Corporation | Substituted diketopiperazine analogs for use as drug delivery agents |
| JP5667095B2 (ja) | 2009-03-11 | 2015-02-12 | マンカインド コーポレイション | 吸入器の抵抗を測定するための装置、システムおよび方法 |
| US8734845B2 (en) | 2009-06-12 | 2014-05-27 | Mannkind Corporation | Diketopiperazine microparticles with defined specific surface areas |
| WO2011056889A1 (en) | 2009-11-03 | 2011-05-12 | Mannkind Corporation | An apparatus and method for simulating inhalation efforts |
| US8383052B2 (en) * | 2010-04-16 | 2013-02-26 | Kellogg Brown & Root Llc | System for a heat balanced FCC forlight hydrocarbon feeds |
| US10023529B2 (en) | 2010-04-30 | 2018-07-17 | Asaki Kasei Chemicals Corporation | Apparatus for removing catalyst surface substances |
| CN105667994B (zh) | 2011-04-01 | 2018-04-06 | 曼金德公司 | 用于药物药盒的泡罩包装 |
| WO2012174472A1 (en) | 2011-06-17 | 2012-12-20 | Mannkind Corporation | High capacity diketopiperazine microparticles |
| IN2014DN03093A (enExample) | 2011-10-24 | 2015-05-15 | Mannkind Corp | |
| CN108057154B (zh) | 2012-07-12 | 2021-04-16 | 曼金德公司 | 干粉药物输送系统和方法 |
| EP2911690A1 (en) | 2012-10-26 | 2015-09-02 | MannKind Corporation | Inhalable influenza vaccine compositions and methods |
| WO2014144895A1 (en) | 2013-03-15 | 2014-09-18 | Mannkind Corporation | Microcrystalline diketopiperazine compositions and methods |
| EP3021834A1 (en) | 2013-07-18 | 2016-05-25 | MannKind Corporation | Heat-stable dry powder pharmaceutical compositions and methods |
| WO2015021064A1 (en) | 2013-08-05 | 2015-02-12 | Mannkind Corporation | Insufflation apparatus and methods |
| US10307464B2 (en) | 2014-03-28 | 2019-06-04 | Mannkind Corporation | Use of ultrarapid acting insulin |
| CN103897744B (zh) * | 2014-03-28 | 2015-11-11 | 新奥科技发展有限公司 | 一种改善流化床设备内流化状况的方法 |
| US9393512B2 (en) | 2014-04-25 | 2016-07-19 | Pall Corporation | Processes for removing entrained particulates from a gas |
| US9168499B1 (en) * | 2014-04-25 | 2015-10-27 | Pall Corporation | Arrangements for removing entrained catalyst particulates from a gas |
| US10561806B2 (en) | 2014-10-02 | 2020-02-18 | Mannkind Corporation | Mouthpiece cover for an inhaler |
| CN109999729B (zh) * | 2019-04-26 | 2022-08-02 | 上海华畅环保设备发展有限公司 | 沸腾床加氢反应器中催化剂原位在线旋流活性恢复方法和装置 |
| CN110052226B (zh) * | 2019-04-26 | 2022-08-02 | 上海华畅环保设备发展有限公司 | 沸腾床加氢反应器中催化剂原位在线旋流活性恢复方法和装置 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2605234A (en) * | 1947-12-01 | 1952-07-29 | Phillips Petroleum Co | Regeneration of a carbonized fischer-tropsch catalyst |
| US2651600A (en) * | 1950-02-21 | 1953-09-08 | Standard Oil Dev Co | Method of reducing contaminants on finely divided catalyst |
| US2958650A (en) * | 1955-07-28 | 1960-11-01 | Houdry Process Corp | Removing contaminants from catalyst particles |
| US3050469A (en) * | 1959-05-25 | 1962-08-21 | Phillips Petroleum Co | Catalyst regeneration process and apparatus |
| JPS61263646A (ja) * | 1985-05-17 | 1986-11-21 | Mitsubishi Heavy Ind Ltd | 石炭焚脱硝触媒の再生方法 |
-
1990
- 1990-11-15 US US07/614,311 patent/US5124291A/en not_active Expired - Lifetime
-
1992
- 1992-04-16 CN CN92103676A patent/CN1046639C/zh not_active Expired - Lifetime
- 1992-04-21 EP EP92303546A patent/EP0566785B1/en not_active Expired - Lifetime
- 1992-04-21 ES ES92303546T patent/ES2097870T3/es not_active Expired - Lifetime
- 1992-04-21 AT AT92303546T patent/ATE149099T1/de not_active IP Right Cessation
- 1992-04-21 DE DE69217650T patent/DE69217650T2/de not_active Expired - Fee Related
- 1992-04-25 TW TW081103266A patent/TW204305B/zh not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| ES2097870T3 (es) | 1997-04-16 |
| TW204305B (enExample) | 1993-04-21 |
| US5124291A (en) | 1992-06-23 |
| CN1046639C (zh) | 1999-11-24 |
| ATE149099T1 (de) | 1997-03-15 |
| EP0566785A1 (en) | 1993-10-27 |
| CN1077399A (zh) | 1993-10-20 |
| EP0566785B1 (en) | 1997-02-26 |
| DE69217650D1 (de) | 1997-04-03 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 8364 | No opposition during term of opposition | ||
| 8327 | Change in the person/name/address of the patent owner |
Owner name: INNOVENE USA LLC (N.D.GES.D.STAATES DELAWARE), CHI |
|
| 8327 | Change in the person/name/address of the patent owner |
Owner name: INEOS USA LLC, WILMINGTON, DEL., US |
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| 8339 | Ceased/non-payment of the annual fee |