US2006223693A1PendingUtilityA1
Catalyst for producing hydrocarbon from synthsis gas and method for producing catalyst
Est. expiryApr 7, 2023(expired)· nominal 20-yr term from priority
B01J 35/40C10G 2/33B01J 23/78B01J 23/75B01J 23/74B01J 37/06B01J 21/08B01J 23/462B01J 23/46B01J 37/34B01J 35/615B01J 35/635B01J 35/638
47
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
A catalyst for Producing hydrocarbon from a syngas is provided. In particular, the catalyst can be composed of catalyst support which a metallic compound is loaded on and that the impurity content of the catalyst is in the range from 0.01 mass % to 0.15 mass %. In addition. a method for producing the catalyst. and a method for producing the hydrocarbon using the catalyst are Provided.
Claims
exact text as granted — not AI-modified1 - 13 . (canceled)
14 . A catalyst for producing hydrocarbon from a syngas, comprising:
a catalyst support on which a metallic compound is loaded, wherein an impurity content of a catalyst is in a range of approximately 0.01 mass % to 0.15 mass %.
15 . The catalyst according to claim 14 , wherein an alkali metal or an alkaline-earth metal content in the catalyst support is in a range of approximately 0.01 mass % to 0.1 mass %.
16 . The catalyst according to claim 15 , wherein the catalyst support simultaneously satisfies a pore diameter in a range of approximately 8 nm to 50 nm, a surface area in a range from 80 m 2 /g to 550 m 2 /g and a pore volume in a range from 0.5 mL/g to 2.0 mL/g.
17 . The catalyst according to claim 14 , wherein the catalyst support simultaneously satisfies a pore diameter in a range of approximately 8 nm to 50 nm, a surface area in a range from 80 m 2 /g to 550 m 2 /g and a pore volume in a range from 0.5 mL/g to 2.0 mL/g.
18 . The catalyst according to claim 14 , wherein the catalyst support allows the catalyst to have a fractured or pulverized ratio of at most 10% when an ultrasonic wave is emitted for a predetermined time period at a room temperature to the catalyst dispersed in water.
19 . The catalyst according to claim 15 , wherein the catalyst support allows the catalyst to have a fractured or pulverized ratio of at most 10% when an ultrasonic wave is emitted for a predetermined time period at a room temperature to the catalyst dispersed in water.
20 . The catalyst according to claim 16 , wherein the catalyst support allows the catalyst to have a fractured or pulverized ratio of at most 10% when an ultrasonic wave is emitted for a predetermined time period at a room temperature to the catalyst dispersed in water.
21 . The catalyst according to claim 14 , wherein the catalyst support is silica having a spherical shape.
22 . The catalyst according to claim 15 , wherein the catalyst support is silica having a spherical shape.
23 . The catalyst according to claim 16 , wherein the catalyst support is silica having a spherical shape.
24 . The catalyst according to claim 17 , wherein the catalyst support is silica having a spherical shape.
25 . The catalyst according to claim 18 , wherein the catalyst support is silica having a spherical shape.
26 . The catalyst according to claim 19 , wherein the catalyst support is silica having a spherical shape.
27 . The catalyst according to claim 20 , wherein the catalyst support is silica having a spherical shape.
28 . The catalyst according to claim 14 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
29 . The catalyst according to claim 15 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
30 . The catalyst according to claim 16 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
31 . The catalyst according to claim 17 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
32 . The catalyst according to claim 18 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
33 . The catalyst according to claim 19 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
34 . The catalyst according to claim 20 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
35 . The catalyst according to claim 21 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
36 . The catalyst according to claim 22 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
37 . The catalyst according to claim 23 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
38 . The catalyst according to claim 24 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
39 . The catalyst according to claim 25 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
40 . The catalyst according to claim 26 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
41 . The catalyst according to claim 27 , wherein the metallic compound contains at least one of iron, cobalt, nickel or ruthenium.
42 . The catalyst according to claim 28 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
43 . The catalyst according to claim 29 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
44 . The catalyst according to claim 30 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
45 . The catalyst according to claim 31 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
46 . The catalyst according to claim 32 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
47 . The catalyst according to claim 33 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
48 . The catalyst according to claim 34 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
49 . The catalyst according to claim 35 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
50 . The catalyst according to claim 36 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
51 . The catalyst according to claim 37 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
52 . The catalyst according to claim 38 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
53 . The catalyst according to claim 39 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
54 . The catalyst according to claim 40 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
55 . The catalyst according to claim 41 , wherein the metallic compound is made from a precursor of metallic compound of at least one of an alkali metal or alkaline-earth metal content of at most 5 mass %.
56 . A method for producing a catalyst which comprises a catalyst support on which a metallic compound is loaded, wherein an impurity content of a catalyst is in a range of approximately 0.01 mass % to 0.15 mass %, the method comprising:
pre-treating the catalyst support to lower an impurity concentration of the catalyst support; and loading the metallic compound on the catalyst support after the pretreatment step.
57 . The method according to claim 56 , wherein the pretreatment step includes rinsing the catalyst support using at least one of acid or an ion-exchanged water.
58 . The method according to claim 56 , further comprising preparing the catalyst using the catalyst support obtained by rinsing water of an alkali metal or alkaline-earth metal content of at most 0.06 mass % during the production of the catalyst support.
59 . The method according to claim 57 , further comprising preparing the catalyst using the catalyst support obtained by rinsing water of an alkali metal or alkaline-earth metal content of at most 0.06 mass % during the production of the catalyst support.
60 . The method according to claim 56 , further comprising shaping the catalyst support to have a spherical shape using a spraying technique.
61 . The method according to claim 57 , further comprising shaping the catalyst support to have a spherical shape using a spraying technique.
62 . The method according to claim 58 , further comprising shaping the catalyst support to have a spherical shape using a spraying technique.
63 . The method according to claim 59 , further comprising shaping the catalyst support to have a spherical shape using a spraying technique.
64 . The method according to claim 56 , wherein the catalyst support is silica.
65 . The method according to claim 57 , wherein the catalyst support is silica.
66 . The method according to claim 58 , wherein the catalyst support is silica.
67 . The method according to claim 59 , wherein the catalyst support is silica.
68 . The method according to claim 60 , wherein the catalyst support is silica.
69 . The method according to claim 61 , wherein the catalyst support is silica.
70 . The method according to claim 62 , wherein the catalyst support is silica.
71 . The method according to claim 63 , wherein the catalyst support is silica.
72 . A method for producing hydrocarbon, comprising:
generating the hydrocarbon from a syngas using a catalyst which is in a range of approximately 0.01 mass % to 0.15 mass %.Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.