GB1223001A - Catalyst carrier and process of making the same - Google Patents
Catalyst carrier and process of making the sameInfo
- Publication number
- GB1223001A GB1223001A GB7781/68A GB778168A GB1223001A GB 1223001 A GB1223001 A GB 1223001A GB 7781/68 A GB7781/68 A GB 7781/68A GB 778168 A GB778168 A GB 778168A GB 1223001 A GB1223001 A GB 1223001A
- Authority
- GB
- United Kingdom
- Prior art keywords
- inorganic
- bonding
- void forming
- void
- materials
- 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
Links
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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2803—Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
-
- 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
- B01J35/34—Mechanical properties
- B01J35/36—Mechanical strength
-
- 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
- B01J35/34—Mechanical properties
- B01J35/38—Abrasion or attrition resistance
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Toxicology (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
Abstract
1,223,001. Porous refractories. SHIKISHIMA MUL-BII K.K. 16 Feb., 1968, No. 7781/68. Heading C1J. [Also in Divisions B1 and C2] A sintered porous catalyst carrier comprises an aggregated inorganic material interconnected by a sintered inorganic bonding material and having a microporous structure comprising voids of size distribution such that a graph of the radius of the void against the cumulative volume of all voids having equal and greater radii is of step-like form and comprises at least 2 steps. Suitable aggreagated inorganic materials are fused alumina, silicon carbide and zircon and suitable bonding materials are fusible clay and porcelain clay. The carrier can be shaped as cylinders, truncated cones, discs, annulii, hollow cylinders, spheres or a shell surrounding an impermeable core of porcelain clay, bauxite and/or mullite. The catalyst carrier is made by (1) forming bonding granules from a pulverulent inorganic material and an inorganic bonding material and coating the bonding granules with an organic surface forming material; (2) mixing the coated bonding granules with pulverulent inorganic aggregate material, pulverized organic void forming material of predetermined size and inorganic bonding material to form aggregate grains; (3) mixing the aggregate grains with pulverized organic void forming material of particle size different from that of the void forming material used in step (2) and inorganic bonding material to form carrier pellets; and (4) sintering the pellets at 1000-1400 F. thereby to convert the organic surface and void forming materials to gaseous substances and to form voids in the pellets. Step (2) can be used to make several batches of aggregate grains, each batch using a void forming material of different particle size so that more steps are formed on the graph. Suitable void forming materials are walnut shell, Indian corn core, cotton yarn waste, woden scobs and styrene resins. In an example the surface and void forming materials used in steps (1), (2) and (3) have increasing sizes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB7781/68A GB1223001A (en) | 1968-02-16 | 1968-02-16 | Catalyst carrier and process of making the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB7781/68A GB1223001A (en) | 1968-02-16 | 1968-02-16 | Catalyst carrier and process of making the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1223001A true GB1223001A (en) | 1971-02-17 |
Family
ID=9839595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB7781/68A Expired GB1223001A (en) | 1968-02-16 | 1968-02-16 | Catalyst carrier and process of making the same |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1223001A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5055442A (en) * | 1989-02-17 | 1991-10-08 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Carrier for catalyst and method for production thereof |
| US5073525A (en) * | 1989-10-23 | 1991-12-17 | Quigley Company, Inc. | Lightweight tundish refractory composition |
-
1968
- 1968-02-16 GB GB7781/68A patent/GB1223001A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5055442A (en) * | 1989-02-17 | 1991-10-08 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Carrier for catalyst and method for production thereof |
| US5073525A (en) * | 1989-10-23 | 1991-12-17 | Quigley Company, Inc. | Lightweight tundish refractory composition |
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