CN101786025A - 用于乙烯固定床氧氯化为1,2-二氯乙烷的催化剂 - Google Patents
用于乙烯固定床氧氯化为1,2-二氯乙烷的催化剂 Download PDFInfo
- Publication number
- CN101786025A CN101786025A CN200911000020A CN200911000020A CN101786025A CN 101786025 A CN101786025 A CN 101786025A CN 200911000020 A CN200911000020 A CN 200911000020A CN 200911000020 A CN200911000020 A CN 200911000020A CN 101786025 A CN101786025 A CN 101786025A
- Authority
- CN
- China
- Prior art keywords
- catalyst granules
- pore volume
- catalyst
- particle
- diameter
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 69
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title claims abstract description 9
- 239000011148 porous material Substances 0.000 claims abstract description 51
- 239000002245 particle Substances 0.000 claims description 36
- 239000008187 granular material Substances 0.000 claims description 24
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 14
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 10
- 229910052783 alkali metal Inorganic materials 0.000 claims description 7
- 150000001340 alkali metals Chemical class 0.000 claims description 7
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 7
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 7
- 150000002910 rare earth metals Chemical class 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 235000011164 potassium chloride Nutrition 0.000 claims description 5
- 239000001103 potassium chloride Substances 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 230000001186 cumulative effect Effects 0.000 claims description 4
- 239000011777 magnesium Substances 0.000 claims description 4
- 229910052700 potassium Inorganic materials 0.000 claims description 4
- 239000011591 potassium Substances 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 3
- 229910052792 caesium Inorganic materials 0.000 claims description 3
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 claims description 3
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 claims description 3
- 229910052749 magnesium Inorganic materials 0.000 claims description 3
- 239000007800 oxidant agent Substances 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 229910052684 Cerium Inorganic materials 0.000 claims description 2
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 1
- 150000002739 metals Chemical class 0.000 claims 1
- 239000008188 pellet Substances 0.000 abstract description 5
- 229910001593 boehmite Inorganic materials 0.000 description 12
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 12
- 239000007864 aqueous solution Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- 230000003197 catalytic effect Effects 0.000 description 5
- ZZBAGJPKGRJIJH-UHFFFAOYSA-N 7h-purine-2-carbaldehyde Chemical compound O=CC1=NC=C2NC=NC2=N1 ZZBAGJPKGRJIJH-UHFFFAOYSA-N 0.000 description 4
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- CEGOLXSVJUTHNZ-UHFFFAOYSA-K aluminium tristearate Chemical compound [Al+3].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CEGOLXSVJUTHNZ-UHFFFAOYSA-K 0.000 description 3
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical class [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 238000000748 compression moulding Methods 0.000 description 3
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011888 foil Substances 0.000 description 3
- JCCNYMKQOSZNPW-UHFFFAOYSA-N loratadine Chemical compound C1CN(C(=O)OCC)CCC1=C1C2=NC=CC=C2CCC2=CC(Cl)=CC=C21 JCCNYMKQOSZNPW-UHFFFAOYSA-N 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000011800 void material Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- ZXKXJHAOUFHNAS-UHFFFAOYSA-N fenfluramine hydrochloride Chemical compound [Cl-].CC[NH2+]C(C)CC1=CC=CC(C(F)(F)F)=C1 ZXKXJHAOUFHNAS-UHFFFAOYSA-N 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002513 implantation Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003643 water by type Substances 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/08—Halides
- B01J27/122—Halides of copper
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/78—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/31—Density
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
- C07C17/15—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
- C07C17/15—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination
- C07C17/152—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons
- C07C17/156—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons of unsaturated hydrocarbons
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- 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
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
本发明涉及用于乙烯固定床氧氯化为1,2-二氯乙烷的中空圆柱形颗粒状催化剂,该催化剂总孔体积为0.4-0.55ml/g,该总孔体积主要由直径为7-50nm的微孔和中孔(其中中孔占主要部分)以及直径为50nm以上直到10,000nm的大孔(以15-35%存在)构成。
Description
技术领域
本发明涉及可用于乙烯固定床氧氯化为1,2-二氯乙烷(DCE)的颗粒状催化剂,该催化剂具有一定的中空圆柱形状和包含在特定范围内的总孔体积,其中直径为7-50nm的中孔是主要部分,并且涉及用于所述催化剂的中空载体。
背景技术
已知的是,乙烯氧氯化为DCE可以在流化床或固定床中进行。在前种情况下,反应器中获得了较为均匀的温度分布,而在另一情形中,虽然反应参数比较容易控制,但由于催化剂颗粒之间以及颗粒与反应气体之间的低交换系数,可产生对催化剂选择性和寿命具有不利影响的局部热点温度。
通常使用中空圆柱状颗粒,该中空圆柱状颗粒由于S/V比率(几何表面积与体积比)高于球体和实心圆柱体的S/V比率,允许获得更有效的热交换和较低的通过催化床的压降,从而获得较好的沿反应床的温度控制和提高的工业反应器产能。
尽管具有以上优点,但必须仔细设计中空圆柱状颗粒,否则若干缺点将变得明显。
例如,如果中空圆柱体的外径和内径之比(De/Di)大于一定值,则颗粒变得过脆,并且催化剂堆密度降低,从而由于较低的活性催化剂相总含量而导致催化床单位体积的转化率降低。
圆柱体的De或者长度增加过高而De/Di维持恒定可引起反应器管内催化剂的不均匀装载和颗粒的可能破坏,导致压降增加。
EP1 053 789 A1中描述了De为4-7mm、Di为2.0-2.8nm、高度为6.1-6.9mm的圆柱形催化剂。
报导该催化剂相对于US P 4740644中所述的长度比外径短的中空圆柱形催化剂和US P 5166120中所述的长度比外径长的催化剂圆柱体是有利的。
在后引述的US专利的催化剂的特征还在于:总孔体积为至少0.6-1.0ml/g,其中不存在小于4nm的孔,并且总孔体积的至少80%由直径为8-20nm的中孔构成,其余为直径大于20nm且至多200nm的孔。
依照EP1 053 789中所考虑的,US P 5166120的催化剂的缺点是具有过高的床空隙分数,这暗示着床中存在较低量的催化材料,导致对于生成DCE而言的较低比产率(g DCE/g催化剂.h),兼有由装载步骤期间催化剂颗粒的破裂引起的高压降。催化剂活性高于孔体积主要由直径小于8nm的孔构成的催化剂的活性。
已知商业中空圆柱形催化剂具有至多0.40ml/g的总孔体积,其中主要部分是微孔和中孔,这种催化剂的产率相当低。
发明内容
本发明的目的是提供一种用于乙烯固定床氧氯化为DCE的中空圆柱形颗粒状催化剂,该催化剂具有相当高的总体积,包含负载在γ氧化铝中空圆柱形颗粒上的氯化铜和选自碱金属、碱土金属及稀土金属的至少一种金属的氯化物,在选择性和转化率及对于生成DCE而言的比产率(g DCE/g催化剂.h)方面具有高的性能,该性能高于具有相同几何参数(形状和大/小)及组成的催化剂。
通过本发明的催化剂达到了该目的及其它目的。
从本发明下面的描述中可显见其它目的。
本发明的催化剂是具有一定几何构型的中空形式的颗粒,包含负载在氧化铝中空圆柱形颗粒上的氯化铜,还优选包含氯化钾,以及任选地包含选自碱金属、碱土金属和稀土金属的至少一种或多种金属的氯化物,该催化剂的特征在于:具有0.4-0.55、优选0.40-0.48ml/g的总孔体积,该总孔体积主要由微孔和中孔构成,其中直径为7-50nm的中孔占主要部分,其余由直径大于50nm且至多10,000nm的大孔构成,该大孔占总体积的15-35%、优选20-35%。平均孔径为10-20nm。总孔体积是指颗粒密度(PD)的倒数和真实密度(RD)的倒数之差(1/PD-1/RD)。
氧化铝载体由d50为约60-65μm,d90约160-165μm和平均直径为70-80μm(激光测定)的勃姆石粉末通过压缩成型制得。
可使用的勃姆石的实例是UOP(USA)制造的商业勃姆石V 700 VERSAL。
这种勃姆石具有如下粒径分布(激光测定):
直径小于 体积%
40μm 34.2
63μm 51.0
100μm 70.4
250μm 99.6
100μm 100
用庞代络(ponderal)筛分法测定的尺寸分布(wt%)是:<63μm 52.1%,63-100μm=24.8%,100-250μm=22.0%,>250μm=1.1%。
可用的勃姆石根据已知方法获得,所述方法通过在控制pH的条件下由NaAlO2水溶液沉淀出Al(OH)3,然后充分洗涤滤出物以尽可能多地除去钠离子。
得自勃姆石V700VERSAL且在600℃和700℃焙烧得到的压制成型中空圆柱形颗粒具有表1中报导的特性,其中还报导了由德国SASOL商业化的勃姆石Pural SCC 150和PURAL SB1的特性。
表1
氧化铝成型载体-形态性质
形状 | 中空圆柱形 | 三叶圆柱形(1) | 中空圆柱形 |
勃姆石 | VersalV700 | VersalV700 | Pural SCC 150 |
润滑剂 | 三硬脂酸铝 | 三硬脂酸铝 | 三硬脂酸铝 |
焙烧℃ | 600 | 700 | 700 |
表面积m2/g | 209 | 164 | 208 |
颗粒密度g/ml | 1.00 | 1.11 | 1.23 |
真实密度g/ml | 3.27 | 3.35 | 3.31 |
总孔体积(2)nm | 0.694 | 0.602 | 0.511 |
平均孔径(3) | 13.3 | 14.7 | 9.8 |
N2吸附-解吸(BET) | |||
m.P.S nm | 9 | 10 | 5.5 |
%孔(D<7nm),基于总孔体积 | 26 | 15 | 63 |
%中孔(8<D<20nm),基于总孔 体积 | 38 | 52 | 8 |
%中孔(8<D<50nm),基于总孔 体积 | 38 | 57 | 10 |
%孔体积(D<7nm),基于中孔 体积(D<50nm) | 33 | 18 | 79 |
水银孔隙率 | |||
大孔孔体积(50<D<10,000nm) ml/g | 0.150 | 0.101 | 0.100 |
%大孔孔体积,基于总孔体积 | 22 | 17 | 20 |
重量100片g | 6.36 | 6.70 | 8.25 |
高度mm | 4.70 | 4.35 | 4.90 |
外径mm | 4.79 | 5.8(4) | 4.65 |
轴向抗压性Kg/片(tabl.) | 73±12 | 80±11 | 86±18 |
径向抗压性Kg/片(tabl). | 2.01±0.35 | 2.36±0.31 | 1.9±0.4 |
(1)三叶圆柱形=具有圆形横截面和叶瓣的颗粒,所述叶瓣具有平行于颗粒轴的通孔,
(2)总孔体积=1/(颗粒密度)-真实密度)
(3)平均孔径=4TV/SA(TV=总体积;SA=表面积)
(4)外切圆周的直径
氧化铝颗粒的总孔体积为0.55-0.75ml/g,并主要由中孔(具有7-50nm直径的孔)和微孔(具有小于7nm直径的孔)构成,其中微孔是次要组分(所述体积的15-45%)。
将获得的成型颗粒(预先在约600-800℃下焙烧以将勃姆石转化为γ氧化铝)用金属氯化物-催化剂组分的水溶液浸渍。优选使用体积稍大于氧化铝颗粒的孔体积的溶液进行浸渍(湿法浸渍)。
催化剂中存在的氯化物的含量,以金属计为3-12wt%Cu,1-4wt%碱金属,0.05-2wt%碱土金属,0.1-3wt%稀土金属。
优选地,Cu含量为4-10wt%,碱金属是钾和/或铯,其用量为0.5-3wt%,碱土金属是镁,其用量是0.05-2wt%,稀土金属是铈,含量为0.5-3wt%。
优选的粒子是圆柱形,具有至少一个与颗粒的轴平行的通孔。De直径为4-6mm,Di直径为1-3mm,高度为4-7mm。
还可以方便地使用具有三叶型横截面的颗粒,其中叶瓣提供有平行于颗粒轴的通孔。
表2报导了本发明催化剂颗粒的代表性性质,表3中报导了用实施例的催化剂获得的催化测试结果。
根据已知的方法,在固定床中使用空气或氧气作为氧化剂,使用本发明的催化剂颗粒将乙烯氧氯化为1,2-二氯乙烷,所处的反应温度为200-300℃,在使用空气时,使用的总原料摩尔比C2H4/HCl/O2是1∶1.99∶0.51,使用氧气时,该摩尔比是1∶0.71∶0.18。
优选地,在使用氧气时,HCl/C2H4、O2/C2H4和HCl/O2的摩尔比分别是0.15-0.50、0.04-0.1和3.20-5.8,该方法在串联的三个反应器中进行,其中第三个反应器装填有由根据本发明的催化剂颗粒构成或包含根据本发明的催化剂颗粒的固定床。
测量
大孔孔体积(具有高于50nm且至多10,000nm直径的孔的体积)由水银(Hg)孔隙度法测量:微孔和中孔的孔体积由BET氮气吸附-解吸法测量(中孔体积=具有2-50nm直径的孔的体积)。
堆密度(也称为表观堆积密度)由ASTM方法D 4164-82测量。
具体实施方式
以下实施例用来阐述本发明,但不限制本发明的范围。
实施例1
将通过如下过程获得的350g De=5mm、Di=2.5mm和高度=5mm的氧化铝中空圆柱体在5L处于室温至50℃的旋转罐中用200ml水溶液浸渍:将混有4wt%三硬酯酸铝的勃姆石Versal V 700粉末压缩成型制得圆柱体,将该圆柱体在600℃下焙烧,所述圆柱体具有209m2/g的S.A.(BET),总孔体积为0.69ml/g,所述水溶液包含:
CuCl2*2H2O=97.0g
KCl=6.9g
MgCl2*6H2O=1.8g
HCl 37wt%=7.0ml
其它=至多230ml的去离子水
将浸渍后的颗粒在烘箱中以如下周期干燥:60℃下1小时,80℃下2小时,100℃下3小时,150℃下16小时。
表2中报导了催化剂颗粒的特性,其中还报导了实施例2以及对比例1和2的催化剂颗粒的特性。
在表3中报导了试验工厂催化剂测试的结果。
实施例2
将通过如下过程获得的300g具有三叶状圆形横截面的氧化铝颗粒用水溶液浸渍(其中各个叶瓣提供有平行于颗粒轴的通孔,并且外切圆周的直径为5.8mm和高度为4.30mm):将混有4wt%三硬酯酸铝的勃姆石Versal V 700粉末压缩成型制得粒料,将该粒料在700℃下焙烧,所述颗粒具有164m2/g的S.A.(BET),总孔体积为0.60ml/g,所述水溶液包含:
CuCl2*2H2O 82.1g
KCl 5.9g
HCl 37wt% 6.0ml
其余是去离子水
按照实施例1中所述将经浸渍的颗粒干燥。
在表2中报导了该催化剂颗粒的特性。
对比例1
将具有与实施例1相同尺寸和形状的400g氧化铝中空圆柱体在5L处于室温的旋转罐中用150ml水溶液浸渍,所述圆柱体通过将混有6wt%三硬酯酸铝的勃姆石Pural SCC 150经压缩成型制得的圆柱形颗粒在700℃下焙烧得到,所述水溶液含有:
CuCl2*2H2O=110.8g
KCl=7.9g
MgCl2*6H2O=2.1g
HCl 37wt%=8.0ml
其余=至多200ml的去离子水。
经浸渍的颗粒按实施例1所述进行干燥。
在表2中报导了该催化剂颗粒的特性。
表3中报导了在与实施例1相同的条件下进行的催化测试的结果。
对比例2
在与实施例1相同的催化剂测试条件下,使用与实施例1的催化剂尺寸和形状相似且具有相似组成的商业催化剂(在表2中报导了其它特性)。
表3中报导了测试结果。
表2催化剂形态性质
催化剂 | 实施例1 | 实施例2 | 对比例1 | 对比例2 |
形状 | 中空圆柱形 | 三叶圆柱形 | 中空圆柱形 | 中空圆柱形 |
Cu wt% | 7.97 | 8.00 | 7.98 | 7.68 |
K wt% | 0.81 | 0.81 | 0.78 | 0.84 |
Mg wt% | 0.05 | - | 0.05 | 0.12 |
表面积m2/g | 123 | 99 | 115 | 102 |
颗粒密度g/ml | 1.29 | 1.37 | 1.55 | 1.78 |
真实密度g/ml | 3.12 | 3.25 | 3.19 | 3.14 |
总孔体积(1)ml/g | 0.455 | 0.422 | 0.332 | 0.243 |
平均孔径nm | 14.8 | 17.1 | 11.5 | 9.5 |
N2吸附-解吸(BET)孔隙率 | ||||
%孔体积(D<7nm),基于总 孔体积 | 20 | 18 | 46 | 66 |
%中孔孔体积(8<D<20nm), 基于总孔体积 | 41 | 51 | 17 | 7 |
%中孔孔体积(8<D<50nm), 基于总孔体积 | 48 | 58 | 20 | 9 |
%孔体积(D<7nm)基于中孔 孔体积(D<50nm) | 29 | 23 | 69 | 88 |
水银孔隙率 | ||||
大孔孔体积(50<D<10,000 nm) ml/g | 0.135 | 0.095 | 0.074 | 0.046 |
%大孔孔体积,基于总孔体 积 | 30 | 23 | 22 | 19 |
MPS(2) | 780 | 281 | 1050 | 480 |
表观密度g/ml | 0.59 | 0.60 | 0.72 | 0.86 |
床空隙分数(3) | 0.54 | 0.56 | 0.54 | 0.52 |
(1)总孔体积=1/(颗粒密度)-(真实密度)
(2)在大孔体积分布曲线最大值处的孔径
(3)床空隙分数=1-表观堆密度/颗粒密度
表3
催化剂性能(冷却剂温度=210℃;压力=0.5巴)
催化剂 | 实施例1 | 实施例2 | 对比例1 | 对比例2 |
催化床高度cm 体积ml | 80 420 | 80 420 | 80 420 | 80 420 |
催化剂载量g 催化剂堆密度g/ml | 246.58 0.59 | 251.2 0.60 | 303.85 0.72 | 360.56 0.86 |
进料总进料Nl/h(*) HCl Nl/h | 771.7 73.3 | 756.0 72.9 | 761.3 70.3 | 772.9 73.5 |
进料摩尔比HCl/C2H4 O2/C2H4 | 0.32 0.09 | 0.31 0.09 | 0.30 0.09 | 0.31 0.09 |
热量 T10cm ℃ 侧面 T20cm ℃ 催化床层 T30cm ℃ T70cm ℃ | 288 315 292 220 | 247 306 303 221 | 269 287 272 220 | 304 317 283 218 |
转化率 HCl%mol | 98.66 | 99.18 | 99.0 | 96.4 |
C2H4摩尔选择性CO% CO2% 纯EDC% | 1.34 1.54 96.73 | 1.09 1.17 97.29 | 1.18 1.46 96.96 | 1.97 1.68 95.93 |
比产率 C2H4到EDC gEDC/ml催化剂.h 参照催化床体积 | 0.38 | 0.38 | 0.37 | 0.37 |
比产率 gEDC/g催化剂.h 参考催化剂重量 | 0.65 | 0.64 | 0.51 | 0.43 |
(*)总进料:C2H4=30.4vol.%,O2=2.7vol.%,HCl=9.5vol.%,N2=57.4vol.%。
Claims (14)
1.一种用于将乙烯氧氯化为1,2-二氯乙烷的中空颗粒状的催化剂颗粒,该催化剂颗粒具有一定的几何构型,包含负载在氧化铝颗粒上的氯化铜,所述催化剂颗粒总孔体积为0.4-0.55ml/g,该总孔体积主要由中孔和微孔构成,其中直径为7-50nm的中孔占主要部分,其余由直径大于50至10,000nm的大孔构成,该大孔占总体积的15-35%。
2.根据权利要求1的催化剂颗粒,其包含以金属计0.5-3wt%的量的氯化钾,和任选的选自除钾以外的碱金属、碱土金属和稀土金属中的一种或多种金属的氯化物,碱金属的量为0.5-3wt%,碱土金属的量为0.05-2wt%,以及稀土金属的量为0.1-3wt%。
3.根据权利要求1或2的催化剂颗粒,其中平均孔径为12-20nm。
4.根据权利要求1-3中任一项的催化剂颗粒,其中总孔体积包含20-35%的大孔体积。
5.根据权利要求1-4中任一项的催化剂颗粒,其中总孔体积是0.40-0.48ml/g并且微孔-中孔孔体积是总孔体积的65-80%。
6.根据权利要求1-5中任一项的催化剂颗粒,其中铜含量为4-10wt%,并且其中碱金属是钾和/或铯,碱土金属是镁,和稀土金属是铈。
7.根据权利要求1-6中任一项的催化剂颗粒,其中钾和/或铯的量为0.5-3wt%,镁的量为0.1-2wt%,和铈的量为0.5-2wt%。
8.根据权利要求1-7中任一项的催化剂颗粒,其中颗粒是外径为4-6mm、内径为1-3mm和高度为4-7mm的中空圆柱体形式。
9.根据权利要求1-8中任一项的催化剂颗粒,其具有三叶状圆柱形横截面,该横截面提供有叶瓣,其每个叶瓣具有平行于颗粒的轴的通孔并且与其它叶瓣的轴等距。
10.由γ氧化铝形成的中空圆柱形颗粒,其总孔体积为0.55-0.75ml/g,主要由直径为至多50nm的微孔-中孔构成,其中直径<7nm的孔占微孔和中孔孔体积的15-45%。
11.根据权利要求10的中空圆柱形颗粒,其提供有一个或多个平行于颗粒的轴的通孔。
12.根据权利要求10和11中任一项所述的中空圆柱形颗粒,其形式是外径为4-6mm,内径为1-3mm和高度为4-7mm的圆柱体。
13.一种将乙烯氧氯化为1,2-二氯乙烷的方法,该方法在固定床中进行,所述固定床由权利要求1-9的催化剂颗粒构成或包含权利要求1-9的催化剂颗粒,该方法使用空气或氧气作为氧化剂,所处的温度为200-300℃,当使用空气时,HCl/C2H4/O2摩尔比是1∶1.99∶0.51,当使用氧气时,HCl/C2H4/O2摩尔比是1∶0.70∶1.79。
14.根据权利要求13的方法,其使用氧气作为氧化剂且在串联的三个反应器中进行,其中第三个反应器装载有固定床,该固定床由根据权利要求1-9的催化剂颗粒构成或包含根据权利要求1-9的催化剂颗粒,其中HCl/C2H4、O2/C2H4和HCl/O2的摩尔比分别是0.15-0.50,0.04-0.10和3.20-5.8。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08172829.7 | 2008-12-23 | ||
EP08172829A EP2208528A1 (en) | 2008-12-23 | 2008-12-23 | Catalysts for fixed bed oxychlorination of ethylene to 1.2-dichloroethane |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101786025A true CN101786025A (zh) | 2010-07-28 |
CN101786025B CN101786025B (zh) | 2015-04-01 |
Family
ID=40688846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN200911000020.4A Expired - Fee Related CN101786025B (zh) | 2008-12-23 | 2009-12-23 | 用于乙烯固定床氧氯化为1,2-二氯乙烷的催化剂 |
Country Status (7)
Country | Link |
---|---|
US (1) | US8216960B2 (zh) |
EP (1) | EP2208528A1 (zh) |
JP (1) | JP2010149115A (zh) |
KR (1) | KR20100074017A (zh) |
CN (1) | CN101786025B (zh) |
BR (1) | BRPI0905169A2 (zh) |
TW (1) | TW201032894A (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103328091A (zh) * | 2010-10-21 | 2013-09-25 | 英尼奥斯欧洲股份公司 | 包含催化剂丸粒和具有预定的尺寸和理化性质的稀释剂珠粒的催化剂体系 |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004299464A (ja) * | 2003-03-28 | 2004-10-28 | Yamaha Motor Co Ltd | 自動二輪車の車体フレーム |
JP6215514B2 (ja) * | 2011-02-21 | 2017-10-18 | 東ソー株式会社 | オキシ塩素化触媒 |
JP5817427B2 (ja) * | 2011-10-21 | 2015-11-18 | 東ソー株式会社 | オキシ塩素化触媒及びそれを用いた1,2−ジクロロエタンの製造方法 |
JP5776492B2 (ja) * | 2011-10-25 | 2015-09-09 | 東ソー株式会社 | オキシ塩素化触媒の製造方法 |
ITMI20112218A1 (it) * | 2011-12-05 | 2013-06-06 | Daniele Malune | Composizione idrosolubile e compressa idrosolubile per l'additivazione di acqua. |
CN103657663B (zh) * | 2012-09-07 | 2016-09-21 | 中国石油化工股份有限公司 | 烯烃氧氯化催化剂及其制备方法和二氯乙烷的制备方法 |
JP2014117673A (ja) * | 2012-12-18 | 2014-06-30 | Tosoh Corp | オキシ塩素化触媒およびそれを用いた1,2−ジクロロエタンの製造方法 |
JP6056457B2 (ja) * | 2012-12-25 | 2017-01-11 | 東ソー株式会社 | 1,2−ジクロロエタンの製造方法 |
TWI642481B (zh) * | 2013-07-17 | 2018-12-01 | 東楚股份有限公司 | Catalyst system for the production of heterogeneous catalysts and 1,2-dichloroethane |
JP6194809B2 (ja) * | 2014-02-05 | 2017-09-13 | 東ソー株式会社 | 1,2−ジクロロエタンの製造方法 |
US9956553B2 (en) | 2016-06-28 | 2018-05-01 | Chevron U.S.A. Inc. | Regeneration of an ionic liquid catalyst by hydrogenation using a macroporous noble metal catalyst |
KR102230989B1 (ko) | 2018-02-23 | 2021-03-23 | 주식회사 엘지화학 | 탄화수소의 옥시클로로화 공정용 촉매, 이의 제조방법 및 이를 이용한 탄화수소의 옥시클로로화 화합물의 제조방법 |
EP3721993B1 (en) | 2018-02-23 | 2022-06-15 | Lg Chem, Ltd. | Catalyst for processing oxychlorination of hydrocarbon, preparation method therefor, and preparation method of oxychlorinated compound of hydrocarbon using same |
CN112154119B (zh) | 2018-03-13 | 2023-12-01 | 株式会社Lg化学 | 烃的部分氧化工艺 |
KR102542195B1 (ko) | 2018-07-20 | 2023-06-09 | 주식회사 엘지화학 | 탄화수소의 부분 산화 공정용 촉매 및 이를 이용한 일산화탄소의 제조방법 |
CN112717907B (zh) * | 2019-10-28 | 2023-10-13 | 武汉理工大学 | 一种纳米片堆积中空球形结构的γ-Al2O3催化剂载体材料及其制备方法 |
JP2022030305A (ja) * | 2020-08-06 | 2022-02-18 | 水澤化学工業株式会社 | アルミナ担体 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4414136A (en) * | 1982-04-02 | 1983-11-08 | Conoco Inc. | Catalysts for ethylene oxychlorination |
US5166120A (en) * | 1990-06-09 | 1992-11-24 | Degussa Aktiengesellschaft | Cylindrically formed catalyst for the oxychlorination of ethylene |
CN1187149A (zh) * | 1995-06-07 | 1998-07-08 | 陶氏化学公司 | 氧氯化的催化剂和方法 |
CN1627989A (zh) * | 2002-02-05 | 2005-06-15 | 巴斯福股份公司 | 用于氧氯化的催化剂组合物 |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1030646B (it) * | 1974-10-04 | 1979-04-10 | Sir Soc Italiana Resine Spa | Procedimento er la produzione di dicloroetano |
DE3046407A1 (de) * | 1980-12-10 | 1982-07-15 | Basf Ag, 6700 Ludwigshafen | Kupfer- und alkalimetalle enthaltender traegerkatalysator und dessen verwendung zur herstellung von 1,2-dichlorethan durch oxichlorierung von ethan |
DE3522474A1 (de) | 1985-06-22 | 1987-01-02 | Basf Ag | Verfahren zur herstellung von 1,2-dichlorethan durch oxichlorierung von ethylen an kupfer enthaltenden traegerkatalysatoren |
IT1274033B (it) * | 1994-04-05 | 1997-07-14 | Montecatini Tecnologie Srl | Catalizzatore in granuli per la sintesi di 1-2 dicloroetano e preprocedimento di ossiclorurazione a letto fisso dell'etilene che utilizza tale catalizzatore. |
IT1282267B1 (it) * | 1995-03-14 | 1998-03-16 | Montecatini Tecnologie Srl | Catalizzatori e supporti per catalizzatori ottenuti per pastigliatura |
DE19751962A1 (de) * | 1997-11-24 | 1999-07-29 | Wacker Chemie Gmbh | Trägerkatalysator, Verfahren zu dessen Herstellung sowie Verwendung bei der Oxichlorierung von Ethylen |
PT1002576E (pt) * | 1998-11-10 | 2004-06-30 | Sued Chemie Mt Srl | Catalisador a base de cobre para oxicloracao de etileno a 1,2-dicloroetano |
EP1053789B1 (en) | 1999-05-21 | 2004-07-14 | Evc Technology Ag | Catalyst and oxychlorination process using it |
DE10009017A1 (de) * | 2000-02-25 | 2001-09-06 | Basf Ag | Geformte Katalysatoren |
ITMI20012241A1 (it) * | 2001-10-25 | 2003-04-25 | Sued Chemie Mt Srl | Catalizzatori per l'ossiclorurazione dell'etilene a 1,2-dicloroetano |
ITMI20030630A1 (it) * | 2003-03-31 | 2004-10-01 | Sued Chemie Mt Srl | Catalizzatori per ossiclorurazione dell'etilene a 1,2-dicloroetano. |
ITMI20042317A1 (it) * | 2004-12-02 | 2005-03-02 | Sued Chemie Mt Srl | Catalizzatori per l'ossiclorurazione dell'etilene a 1,2-dicloroetano |
-
2008
- 2008-12-23 EP EP08172829A patent/EP2208528A1/en not_active Withdrawn
-
2009
- 2009-12-11 TW TW098142411A patent/TW201032894A/zh unknown
- 2009-12-16 BR BRPI0905169-4A patent/BRPI0905169A2/pt active Search and Examination
- 2009-12-18 US US12/641,624 patent/US8216960B2/en active Active
- 2009-12-18 KR KR1020090126977A patent/KR20100074017A/ko not_active Application Discontinuation
- 2009-12-22 JP JP2009290827A patent/JP2010149115A/ja active Pending
- 2009-12-23 CN CN200911000020.4A patent/CN101786025B/zh not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4414136A (en) * | 1982-04-02 | 1983-11-08 | Conoco Inc. | Catalysts for ethylene oxychlorination |
US5166120A (en) * | 1990-06-09 | 1992-11-24 | Degussa Aktiengesellschaft | Cylindrically formed catalyst for the oxychlorination of ethylene |
CN1187149A (zh) * | 1995-06-07 | 1998-07-08 | 陶氏化学公司 | 氧氯化的催化剂和方法 |
CN1627989A (zh) * | 2002-02-05 | 2005-06-15 | 巴斯福股份公司 | 用于氧氯化的催化剂组合物 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103328091A (zh) * | 2010-10-21 | 2013-09-25 | 英尼奥斯欧洲股份公司 | 包含催化剂丸粒和具有预定的尺寸和理化性质的稀释剂珠粒的催化剂体系 |
Also Published As
Publication number | Publication date |
---|---|
CN101786025B (zh) | 2015-04-01 |
JP2010149115A (ja) | 2010-07-08 |
EP2208528A1 (en) | 2010-07-21 |
US20100160697A1 (en) | 2010-06-24 |
KR20100074017A (ko) | 2010-07-01 |
EP2208528A8 (en) | 2010-11-17 |
US8216960B2 (en) | 2012-07-10 |
TW201032894A (en) | 2010-09-16 |
BRPI0905169A2 (pt) | 2011-03-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101786025B (zh) | 用于乙烯固定床氧氯化为1,2-二氯乙烷的催化剂 | |
CA2611093C (en) | A catalyst, a process for preparing the catalyst, and a process for the production of an olefin oxide, a 1,2-diol, a 1,2-diol ether, or an alkanolamine | |
US7825062B2 (en) | Catalyst carrier and a process for preparing the catalyst carrier | |
CN101786007A (zh) | 用于乙烯氧氯化为1.2-二氯乙烷的催化剂 | |
Zhao et al. | An Au–Cu bimetal catalyst for acetylene hydrochlorination with renewable γ-Al 2 O 3 as the support | |
CN105392561A (zh) | 非均相催化剂和1,2-二氯乙烷的制造用催化剂体系 | |
JP2013545597A (ja) | 所定の寸法及び物理化学的性質を有する触媒ペレット及び希釈用ビーズを含む触媒系 | |
JP2012513884A (ja) | エチレンのジクロロエタンへのオキシ塩素化用の触媒の前駆体 | |
CN112705271B (zh) | 中空球形载体及其制备方法与应用 | |
WO2018136381A1 (en) | Silver impregnation method for producing ethylene oxide catalyst with enhanced catalytic ability | |
CN112705215B (zh) | 核壳型催化剂及其制备方法与应用 | |
WO2024079247A1 (en) | Epoxidation catalyst | |
CN112691680A (zh) | 丙烯醛合成用复合催化剂及其制备方法与应用 | |
CN117482936A (zh) | 一种氧化铝小球、制备方法及催化重整催化剂 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150401 Termination date: 20171223 |
|
CF01 | Termination of patent right due to non-payment of annual fee |