JP2009142811A - 触媒を再生させる装置および方法 - Google Patents
触媒を再生させる装置および方法 Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 151
- 238000000034 method Methods 0.000 title claims abstract description 9
- 230000001172 regenerating effect Effects 0.000 title claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000003546 flue gas Substances 0.000 claims abstract description 35
- 230000008929 regeneration Effects 0.000 claims description 35
- 238000011069 regeneration method Methods 0.000 claims description 35
- 239000007789 gas Substances 0.000 claims description 27
- 239000000567 combustion gas Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 description 16
- 239000000571 coke Substances 0.000 description 15
- 238000006243 chemical reaction Methods 0.000 description 14
- 229930195733 hydrocarbon Natural products 0.000 description 14
- 150000002430 hydrocarbons Chemical class 0.000 description 14
- 238000002485 combustion reaction Methods 0.000 description 13
- 238000000926 separation method Methods 0.000 description 10
- 238000004231 fluid catalytic cracking Methods 0.000 description 9
- 230000032258 transport Effects 0.000 description 9
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 238000005243 fluidization Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000011275 tar sand Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- 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
-
- 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
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- 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
- B01J8/0065—Separating solid material from the gas/liquid stream by impingement against stationary members
-
- 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
- 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
- B01J8/1872—Details of the fluidised bed reactor
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- 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
- B01J8/26—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 two or more fluidised beds, e.g. reactor and regeneration installations
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- 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
- B01J8/26—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 two or more fluidised beds, e.g. reactor and regeneration installations
- B01J8/28—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 two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/70—Catalyst aspects
- C10G2300/708—Coking aspect, coke content and composition of deposits
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
【解決手段】離脱デバイスの離脱アームは、アームを取り巻く外シェルと、触媒および煙道ガスがアームを出ることを可能にするスロットを有する内シェルと、外壁の開口よりも下方に位置する下縁を有する外側バッフルとを含む。このバッフルは、触媒および煙道ガスを下方へ導き、半径方向流を限定する。触媒および煙道ガスは、上昇管部の外壁の開口を通って、第1の空塔速度で離脱アームに入り、離脱アームの底部のスロットから、第1の空塔速度の1.33倍以下の速度で出ていく。
【選択図】図1
Description
12 再生器スタンドパイプ
14 滑り弁
16 ノズル
18 上昇管
20 供給原料噴射ノズル
22 離脱アーム
24 ポート
26 離脱容器
28 輸送導管
30 サイクロン
32 分離容器
34 収集室
36 出口ノズル
38 ディップレッグ
40 ストリッピング部
42 ポート
43 バッフル
44 バッフル
46 入口
48 反応器導管
50 再生容器
52 滑り弁
54 第1の室ないし下室
56 第1の室ないし下室の外壁
57 移行部
58 燃焼部
59 高密度触媒床
60 上昇管部
61 上昇管部の外壁
62 使用済み触媒入口シュート
63 入口シュート
64 導管
64 キャップ
66 分配器
67 外部再循環スタンドパイプ
68 分配器の開口
69 制御弁
70 離脱デバイス
70’ 離脱デバイス
70” 離脱デバイス
72 離脱アーム
72’ 離脱アーム
74 開口
76 上昇管部の外壁の開口
78 凹み
80 外シェル
81 離脱アームの側壁
82 離脱アームの側壁
84 内シェル
86 スロット
88 水平部分
89 転向部分
90 垂直外バッフル部分
90’ 垂直外バッフル部分
92 バンド
94 垂直バッフル部分の下縁
98 サイクロン分離器
99 サイクロン分離器
100 上室ないし第2の室
101 第2の室の側壁
106 流動化導管
108 流動化分配器
110 出口導管
112 ディップレッグ
113 ディップレッグ
114 出口
Claims (10)
- 触媒の炭素質付着物を燃焼させる触媒再生容器であって、
炭素質付着物を有する使用済み触媒を第1の室に供給する触媒入口と、少なくとも部分的に再生された触媒を提供し、煙道ガスを発生させるために、前記使用済み触媒と接触させ、炭素質付着物を燃焼させる燃焼ガスを第1の室内に分配する燃焼ガス分配器とを含む第1の室と、
前記第1の室から延びる、再生された触媒および煙道ガスを輸送する上昇管部であって、外壁と、前記外壁の少なくとも1つの開口と、前記開口を取り巻いて、前記外壁から半径方向に延びる少なくとも1つの離脱アームとを含み、前記離脱アームが、前記アームを取り巻く外シェルと、触媒および煙道ガスが前記アームを出ることを可能にするスロットを有する内シェルと、前記外壁の前記開口よりも下方に位置する下縁を有する垂直バッフルとを含み、前記垂直バッフルが、前記触媒および煙道ガスを下方へ導き、半径方向流を最小限に抑える上昇管部と、
前記離脱アームをその内部に含み、燃焼ガスから触媒を分離するサイクロン分離器と、再生触媒出口と、煙道ガス出口とを含む第2の室と
を含む触媒再生容器。 - 前記アームの前記スロットの面積と前記開口の面積との比が0.75から2.5の間である、請求項1に記載の触媒再生容器。
- 前記離脱アームの前記外シェルが前記垂直バッフルを含み、下方へ曲げられた半パイプを画定した、請求項1に記載の容器。
- 前記外シェルが、水平部分と、前記垂直バッフルと連続した転向部分とを含む、請求項3に記載の容器。
- 前記スロットが、前記外シェルの前記水平部分の垂直方向下方の前記内シェル内に画定された、請求項4に記載の容器。
- 前記スロットが、前記内シェルの外縁と前記垂直バッフルの内面との間に画定された、請求項5に記載の容器。
- 前記垂直バッフルが半円筒を画定した、請求項1に記載の容器。
- 前記外バッフルの前記下縁が、前記外壁の前記開口よりも、前記開口の垂直高さの少なくとも半分の距離だけ下方に位置する、請求項1に記載の容器。
- 半径方向のガス流を妨げる追加のバッフルをさらに含む、請求項1に記載の容器。
- 使用済み触媒を再生させる方法であって、
炭素質付着物を有する使用済み触媒を触媒再生容器の第1の室に供給するステップと、
前記第1の室に燃焼ガスを分配するステップと、
前記使用済み触媒と燃焼ガスとを接触させるステップと、
前記使用済み触媒の炭素質付着物を燃焼させるステップと、
少なくとも部分的に再生された触媒を提供するステップと、
煙道ガスを発生させるステップと、
前記再生された触媒および前記煙道ガスを、前記第1の室から上昇管部の中へ輸送するステップと、
触媒および煙道ガスを、前記上昇管部の外壁の開口を通して、前記外壁から半径方向に延びる離脱アーム内に第1の空塔速度で放出するステップと、
触媒および煙道ガスを、前記離脱アームのスロットを通して、前記第1の空塔速度の1.33倍以下の第2の空塔速度で放出するステップと、
前記再生された触媒を前記煙道ガスから離脱させるステップと
を含む方法。
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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US11/950,909 | 2007-12-05 | ||
US11/950,886 US7799287B2 (en) | 2007-12-05 | 2007-12-05 | Apparatus and process for regenerating catalyst |
US11/950,886 | 2007-12-05 | ||
US11/950,909 US7902101B2 (en) | 2007-12-05 | 2007-12-05 | Process for regenerating catalyst |
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Cited By (4)
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JP2017534717A (ja) * | 2014-10-09 | 2017-11-24 | サウジ アラビアン オイル カンパニー | 化学ループの概念を取り入れた重質液体燃料のコークス化 |
JP7449414B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | コークス制御反応器、含酸素化合物から軽オレフィンを製造する装置及び応用 |
JP7449415B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | 流動床再生器、軽オレフィンを調製する装置およびその応用 |
JP7449413B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | 流動床反応器、装置及び含酸素化合物から軽オレフィンを製造する方法 |
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CN102814151B (zh) * | 2011-06-08 | 2014-02-26 | 富德(北京)能源化工有限公司 | 由含氧化合物制烯烃的流化床反应器和方法 |
US9073030B2 (en) * | 2013-08-21 | 2015-07-07 | Uop Llc | Apparatuses and risers for reacting feedstock in the presence of catalyst and methods for installing baffles in risers |
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Cited By (5)
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JP2017534717A (ja) * | 2014-10-09 | 2017-11-24 | サウジ アラビアン オイル カンパニー | 化学ループの概念を取り入れた重質液体燃料のコークス化 |
US10125323B2 (en) | 2014-10-09 | 2018-11-13 | Saudi Arabian Oil Company | Integrated heavy liquid fuel coking with chemical looping concept |
JP7449414B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | コークス制御反応器、含酸素化合物から軽オレフィンを製造する装置及び応用 |
JP7449415B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | 流動床再生器、軽オレフィンを調製する装置およびその応用 |
JP7449413B2 (ja) | 2020-10-16 | 2024-03-13 | 中国科学院大▲連▼化学物理研究所 | 流動床反応器、装置及び含酸素化合物から軽オレフィンを製造する方法 |
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JP6084271B2 (ja) | 2017-02-22 |
JP2013212507A (ja) | 2013-10-17 |
JP5449753B2 (ja) | 2014-03-19 |
EP2070592A3 (en) | 2012-01-18 |
EP2070592A2 (en) | 2009-06-17 |
JP2016026114A (ja) | 2016-02-12 |
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