CN107413390A - 一种新型催化裂化催化剂载体及其制备方法 - Google Patents
一种新型催化裂化催化剂载体及其制备方法 Download PDFInfo
- Publication number
- CN107413390A CN107413390A CN201710328043.6A CN201710328043A CN107413390A CN 107413390 A CN107413390 A CN 107413390A CN 201710328043 A CN201710328043 A CN 201710328043A CN 107413390 A CN107413390 A CN 107413390A
- Authority
- CN
- China
- Prior art keywords
- catalytic cracking
- cracking catalyst
- catalyst carrier
- acid
- flyash
- 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 63
- 238000004523 catalytic cracking Methods 0.000 title claims abstract description 35
- 238000002360 preparation method Methods 0.000 title claims description 17
- 235000019198 oils Nutrition 0.000 claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- 239000010881 fly ash Substances 0.000 claims abstract description 16
- 239000003921 oil Substances 0.000 claims abstract description 15
- 239000000295 fuel oil Substances 0.000 claims abstract description 10
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- 238000009826 distribution Methods 0.000 claims abstract description 7
- 239000011148 porous material Substances 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 7
- 230000003750 conditioning effect Effects 0.000 claims abstract description 4
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 3
- 239000012876 carrier material Substances 0.000 claims abstract 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims 4
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 claims 1
- KBIWNQVZKHSHTI-UHFFFAOYSA-N 4-n,4-n-dimethylbenzene-1,4-diamine;oxalic acid Chemical compound OC(=O)C(O)=O.CN(C)C1=CC=C(N)C=C1 KBIWNQVZKHSHTI-UHFFFAOYSA-N 0.000 claims 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 claims 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims 1
- 235000015165 citric acid Nutrition 0.000 claims 1
- 239000001630 malic acid Substances 0.000 claims 1
- 235000011090 malic acid Nutrition 0.000 claims 1
- 150000007522 mineralic acids Chemical class 0.000 claims 1
- 238000012986 modification Methods 0.000 claims 1
- 230000004048 modification Effects 0.000 claims 1
- 229910017604 nitric acid Inorganic materials 0.000 claims 1
- 150000007524 organic acids Chemical class 0.000 claims 1
- 235000006408 oxalic acid Nutrition 0.000 claims 1
- 235000011007 phosphoric acid Nutrition 0.000 claims 1
- 239000012756 surface treatment agent Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000010883 coal ash Substances 0.000 abstract description 5
- 238000012545 processing Methods 0.000 abstract description 5
- 239000002910 solid waste Substances 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 description 13
- 238000005336 cracking Methods 0.000 description 11
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 9
- 239000007787 solid Substances 0.000 description 9
- 239000005995 Aluminium silicate Substances 0.000 description 7
- 235000012211 aluminium silicate Nutrition 0.000 description 7
- 239000002808 molecular sieve Substances 0.000 description 7
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 230000032683 aging Effects 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 6
- 229910001593 boehmite Inorganic materials 0.000 description 6
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000009102 absorption Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000005360 mashing Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000013335 mesoporous material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 101150116295 CAT2 gene Proteins 0.000 description 1
- 101100326920 Caenorhabditis elegans ctl-1 gene Proteins 0.000 description 1
- 101100494773 Caenorhabditis elegans ctl-2 gene Proteins 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000331528 Chlorophytum capense Species 0.000 description 1
- 101100112369 Fasciola hepatica Cat-1 gene Proteins 0.000 description 1
- 244000261422 Lysimachia clethroides Species 0.000 description 1
- 101100005271 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) cat-1 gene Proteins 0.000 description 1
- 101100005280 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) cat-3 gene Proteins 0.000 description 1
- 101100126846 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) katG gene Proteins 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 230000001147 anti-toxic effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002872 contrast media Substances 0.000 description 1
- 150000001924 cycloalkanes Chemical class 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052622 kaolinite Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- -1 stirs 30min Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 239000010913 used oil 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/12—Silica and 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- B01J35/615—
-
- B01J35/633—
-
- B01J35/635—
-
- B01J35/638—
-
- B01J35/647—
-
- B01J35/651—
-
- 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
- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1081—Alkanes
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1096—Aromatics or polyaromatics
-
- 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
Abstract
本发明涉及催化剂载体技术领域,同时也是固体废弃物处理应用领域,具体是一种由粉煤灰制备新型催化裂化催化剂载体的研究技术。该方法采用表面处理剂对粉煤灰进行改性处理后得到具有高比表面、高稳定性和介孔分布范围广的催化剂载体材料,这种载体材料化学性质稳定,孔径为3‑60nm,介孔主要集中于5‑20nm,比表面为130‑350cm2/g,孔体积为0.1‑2.0cm2/g,在催化裂化催化剂结构中提供中等大小的孔道,能裂解大中等油分子,提高重油、渣油等劣质油品向轻质油品的转化率,具有较好的应用推广前景。
Description
技术领域
本发明涉及催化裂化催化剂载体技术领域,同时也是固体废弃物处理应用领域,具体是一种由粉煤灰制备新型催化裂化催化剂载体的研究技术。
背景技术
催化剂主要由载体(基质)、粘结剂、活性组分三部分组成,其中载体主要用于支持活性组分,使活性组分分散在其表面上,并能为催化剂增加有效表面和提供合适的孔结构、提高催化剂的水热稳定性和机械强度、增加催化剂的抗毒性能等作用。
载体自身物化性能的不同,其在催化剂中的影响程度也不同。根据IUPAC的分级标准,在FCC催化剂中要存在三种不同类型的孔:微孔、介孔和大孔。其中,由活性组分提供孔径小于2nm的微孔,主要为烃类的裂化提供反应活性位,即对裂化起关键作用的分子筛作为提供微孔的材料,烃类需进入分子筛的内部方可得到裂化形成小分子。然而,由于重油组分中因其自身的支链多、结构复杂等特点导致其分子太大(动力学直径在3-10nm之间),不能直接进入微孔进行裂解反应。重油大分子的预裂解反应通常在小颗粒空隙间形成的大孔(> 50nm)进行。介于大孔与微孔之间的介孔通常用于将环烷烃和芳香烃的侧链裂解成轻烃和轻循环油(柴油),但催化剂中介孔的数量是有限的。
关于催化裂化催化剂载体的研究报道有很多,如专利CN1210031A公开了一种催化裂化催化剂载体的改性方法,将高岭土与硫酸铵的混合物于高温下焙烧后水洗得到改姓后的高岭土,以改性后的高岭土为载体制备的催化裂化催化剂具有更高的重油转化能力,更高的活性和汽油选择性。专利CN104549541A公开了一种重油催化裂化催化剂载体的制备方法,该方法在催化剂载体的制备过程中加入至少两种硅源,将粘土、氧化铝和氧化硅按照一定的比例进行混合并经过一定的过程,最终得到具有利于重油裂化的优质孔道分布的催化裂化催化剂。
随着电力工业的发展,燃煤电厂的粉煤灰排放量逐年增加,成为我国当前排量较大的工业废渣之一。大量的粉煤灰不加处理,就会产生扬尘,污染大气;若排入水系会造成河流淤塞,而其中的有毒化学物质还会对人体和生物造成危害。
目前,粉煤灰各电厂炼厂产生的粉煤灰,它们大部分是铝、硅,还有少量的Ti、Fe等金属。
研究表明,目前主要的处理方式为掩埋或是做建筑用材,也有一些提取其中的有用物质,合成其它材料等研究,但是这些研究很少能实现其各种元素的分离与单独应用,限制了粉煤灰的再利用领域,且未有将处理后的粉煤灰应用于催化裂化催化剂的制备过程中的报道。
本发明根据粉煤灰的成分构成,将其进行改姓处理得到具有较宽的孔径分布的新型催化裂化催化剂载体,并考察了其应用于催化渣油裂化催化剂中的催化性能,因此这种资源化利用方式具有明显的经济效益和应用前景。
发明内容
本发明的目的在于提供一种新型催化裂化催化剂载体及其的制备方法,该载体是具有高比表面、强吸附性能和介孔分布范围广的硅质介孔材料,这种硅质介孔材料性质稳定,孔径为3-60nm,介孔主要集中于5-20nm,比表面为130-350cm2/g,孔体积为0.2-2.0cm2/g,在催化裂化催化剂结构中提供中等大小的孔道,能裂解大、中等油分子,提高重油、渣油等劣质油品向轻质油品的转化率。
本发明所提供的催化裂化催化剂载体的制备方法包括以下几个步骤:
(1)将粉煤灰与双氧水、水一起打浆,搅拌30min,粉煤灰:双氧水=1:0.1-0.5
(2)按照pH=0-3,固液比1:2-10的比例加入表面处理剂;
(3)加表面处理剂后调节反应温度为90-150℃,在此温度下反应1-6h;
(4)反应结束后离心过滤得到滤饼,对滤饼进行洗涤,直至化学组成不变为止,然后干燥后采用球磨机将其磨至粒径<5微米后得到新型催化裂化催化剂载体。
本发明的优势在于:由该方法得到的催化裂化催化剂载体具有很好的吸附性能和担载性能,其孔径分布范围广,裂解中大型油分子能力强,并且该种制备方法简单易行,既提供了一种新型的制备催化裂化催化剂载体的方法,又增加了粉煤灰的处理应用领域。
具体实施方式
为方便说明和解释,本次发明中所制备的新型载体在催化裂化催化剂的制备过程中代替部分拟薄水铝石,在实际的应用过程中并不限定于本发明中所提,也可以代替高岭土。
本发明中采用以下分析方法对制备得到的催化剂的物化性能和裂化反应性能进行分析与评价:
(1)磨损指数:鹅颈管法,RIPP。
(2)比表面:氮气吸附仪,美国康塔公司生产。实验采用QUADRASORB SI型物理吸附仪进行样品比表面和孔结构分析表征。测量前将催化剂在300℃真空处理3h,然后在液态氮温度77K对高纯氮进行吸附和脱附。
(3)粒度分布:马尔文激光粒度仪。
(4)催化剂老化:采用北京威肯杜科技有限公司生产的催化剂水汽老化装置对不同催化剂进行800℃/4h的老化。
(5)催化剂性能评价:微反活性采用北京威肯杜科技有限公司生产的MAT-11催化剂微反实验装置测定,反应原料为大港直馏轻柴油(馏分235-337℃),反应温度460℃,反应时间70s,催化剂装量5g,进油量1.56g。反应尾气用冰浴冷凝管收集,计算出液收量。反应性能采用北京威肯杜科技有限公司生产的重油微反装置进行评价,使用装置所用原料油作为评价用原料油,老化剂装填量5.0g,裂化气组成通过在线气相色谱仪分析,液体产物的烃类组成通过离线色谱仪分析。
实施例1
(1)新型催化裂化催化剂载体的制备:将3010g粉煤灰与3920g水和600g双氧水混合打浆30min后形成均匀一致的浆液;加入4013g浓硫酸后密闭,加热至120℃,反应3h后卸压卸料并采用离心的方式将反应后得到的固液混合物进行固液分离;将分离得到的固体采用去离子水洗涤,洗至固体中的组成含量不变为止,干燥后采用球磨机将其磨至DV0.5=3.2,得到样品1。
(2)按照高岭土:拟薄水铝石:样品1:铝溶胶:分子筛=33:19:3:10:35的比例,酸铝比=0.06进行打浆、喷雾干燥后得到催化剂1,标记为cat-1。
实施例2
(1)新型催化裂化催化剂载体的制备:将3010g粉煤灰与3920g水和500g双氧水混合打浆30min后形成均匀一致的浆液;加入4213g浓硫酸后密闭,加热至140℃,反应3h后卸压卸料并采用离心的方式将反应后得到的固液混合物进行固液分离;将分离得到的固体采用去离子水洗涤,洗至固体中的组成含量不变为止,干燥后采用球磨机将其磨至DV0.5=2.9,得到样品2。
(2)按照高岭土:拟薄水铝石:样品2:铝溶胶:分子筛=33:17:5:10:35的比例,酸铝比=0.06进行打浆、喷雾干燥后得到催化剂2,标记为cat-2。
实施例3
(1)新型催化裂化催化剂载体的制备:将3010g粉煤灰与3920g水和200g双氧水混合打浆30min后形成均匀一致的浆液;加入3958g浓硫酸后密闭,加热至120℃,反应3h后卸压卸料并采用离心的方式将反应后得到的固液混合物进行固液分离;将分离得到的固体采用去离子水洗涤,洗至固体中的组成含量不变为止,干燥后采用球磨机将其磨至DV0.5=4.1,得到样品3。
(2)催化裂化催化剂的制备:按照高岭土:拟薄水铝石:样品3:铝溶胶:分子筛=33: 19:8:10:35的比例,酸铝比=0.06进行打浆、喷雾干燥后得到催化剂3,标记为cat-3。
对比例1
(1)催化裂化催化剂的制备:按照高岭土:拟薄水铝石:铝溶胶:分子筛=33:22:10: 35的比例,酸铝比=0.06进行打浆、喷雾干燥后得到催化剂1,标记为DB-1。
(2)催化裂化催化剂的制备:按照高岭土:拟薄水铝石:铝溶胶:分子筛=34:21:10: 35的比例,酸铝比=0.06进行打浆、喷雾干燥后得到催化剂1,标记为DB-2。
对不同的催化裂化催化剂进行物化性质的分析,结果见表1和表2。
表1不同催化裂化催化剂的性质分析
表2不同催化裂化催化剂的粒度分析数据
采用北京威肯杜科技有限公司生产的重油微反装置进行评价,使用装置所用原料油作为评价用原料油,原料油的数据见表3。加入吊兰老化后的老化剂5.0g,裂化气组成通过在线气相色谱仪分析,液体产物的烃类组成通过离线色谱仪分析。
表3原料油的分析数据
表4不同催化剂的催化性能评价
从表4可以看出采用粉煤灰制备的催化裂化催化剂载体应用于催化剂的制备上,最终得到的催化裂化催化剂其总液收和轻油收率均高于对比剂,且具有明显的裂解重油大分子的能力,说明这种由粉煤灰制备的催化裂化催化剂载体能显著提升催化剂的重油和渣油转化率。
Claims (4)
1.一种新型催化裂化催化剂载体及其制备方法,其特征在于:利用粉煤灰作为原料,以表面处理剂为改性剂,将粉煤灰改性为具有高比表面、宽孔径分布且具有高稳定性能的载体材料,这种载体材料化学性质稳定,孔径为3-60nm,介孔主要集中于5-20nm,比表面为130-350cm2/g,孔体积为0.2-2.0cm2/g,在催化裂化催化剂结构中提供中等大小的孔道,能裂解大、中等油分子,提高重油、渣油等劣质油品向轻质油品的转化率。
2.按照权利要求1所述的新型催化裂化催化剂载体材料,其特征在于:所述的粉煤灰的主要成分为氧化硅和氧化铝。
3.按照权利要求1所述的新型催化裂化催化剂载体材料,其特征在于:所述的表面处理剂为双氧水和盐酸、硫酸、硝酸、磷酸等无机酸与柠檬酸、草酸、苹果酸、乙二酸等有机酸中的一种或几种的混合液。
4.按照权利要求1中所述的新型催化裂化催化剂载体材料,其特征在于:所述的改性处理的条件为pH=0-3,温度90-150℃,固液比1:2-6,时间为1-6h。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710328043.6A CN107413390B (zh) | 2017-05-11 | 2017-05-11 | 一种新型催化裂化催化剂载体及其制备方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710328043.6A CN107413390B (zh) | 2017-05-11 | 2017-05-11 | 一种新型催化裂化催化剂载体及其制备方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107413390A true CN107413390A (zh) | 2017-12-01 |
CN107413390B CN107413390B (zh) | 2021-06-01 |
Family
ID=60425826
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710328043.6A Active CN107413390B (zh) | 2017-05-11 | 2017-05-11 | 一种新型催化裂化催化剂载体及其制备方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107413390B (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272764A (zh) * | 2019-06-04 | 2019-09-24 | 新奥科技发展有限公司 | 一种半焦飞灰改性剂的制备方法以及半焦飞灰的利用方法 |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1994552A (zh) * | 2006-12-13 | 2007-07-11 | 大连理工大学 | 改性粉煤灰吸附剂及处理硝基酚类阻聚剂生产废水的方法 |
CN102824849A (zh) * | 2012-08-03 | 2012-12-19 | 东北石油大学 | 一种降低FCC再生过程中NOx排放的方法 |
CN103084143A (zh) * | 2013-01-28 | 2013-05-08 | 安徽工程大学 | 一种双孔沸石微球及其制备方法 |
CN103272626A (zh) * | 2013-05-31 | 2013-09-04 | 南京大学 | 一种以粉煤灰漂珠为基体固载杂多酸的复合催化剂、其制备方法和应用 |
CN104030306A (zh) * | 2014-05-16 | 2014-09-10 | 茂名市茂群高岭土有限公司 | 一种用于全白土型催化裂化催化剂的高岭土 |
CN104069797A (zh) * | 2014-07-22 | 2014-10-01 | 青岛博睿林新材料有限公司 | 一种利用氨水改性炉渣吸附甲醛的吸附剂 |
CN104096534A (zh) * | 2014-07-22 | 2014-10-15 | 青岛博睿林新材料有限公司 | 一种二次改性炉渣吸附甲醛的吸附剂 |
CN104150855A (zh) * | 2014-07-18 | 2014-11-19 | 西安建筑科技大学 | 一种粉煤灰基介孔材料及其制备方法 |
CN104353503A (zh) * | 2014-11-12 | 2015-02-18 | 中国海洋石油总公司 | 一种球形硅铝复合载体的制备方法 |
CN105749867A (zh) * | 2016-04-27 | 2016-07-13 | 常州市好利莱光电科技有限公司 | 一种复合改性粉煤灰制备含铜废水处理剂的方法 |
CN105778979A (zh) * | 2014-12-22 | 2016-07-20 | 中国石油天然气股份有限公司 | 一种降低催化裂化汽油硫含量的催化剂及其制备方法 |
CN106000276A (zh) * | 2016-06-30 | 2016-10-12 | 青岛惠城环保科技股份有限公司 | 一种新型硅质介孔材料及其制备方法 |
-
2017
- 2017-05-11 CN CN201710328043.6A patent/CN107413390B/zh active Active
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1994552A (zh) * | 2006-12-13 | 2007-07-11 | 大连理工大学 | 改性粉煤灰吸附剂及处理硝基酚类阻聚剂生产废水的方法 |
CN102824849A (zh) * | 2012-08-03 | 2012-12-19 | 东北石油大学 | 一种降低FCC再生过程中NOx排放的方法 |
CN103084143A (zh) * | 2013-01-28 | 2013-05-08 | 安徽工程大学 | 一种双孔沸石微球及其制备方法 |
CN103272626A (zh) * | 2013-05-31 | 2013-09-04 | 南京大学 | 一种以粉煤灰漂珠为基体固载杂多酸的复合催化剂、其制备方法和应用 |
CN104030306A (zh) * | 2014-05-16 | 2014-09-10 | 茂名市茂群高岭土有限公司 | 一种用于全白土型催化裂化催化剂的高岭土 |
CN104150855A (zh) * | 2014-07-18 | 2014-11-19 | 西安建筑科技大学 | 一种粉煤灰基介孔材料及其制备方法 |
CN104069797A (zh) * | 2014-07-22 | 2014-10-01 | 青岛博睿林新材料有限公司 | 一种利用氨水改性炉渣吸附甲醛的吸附剂 |
CN104096534A (zh) * | 2014-07-22 | 2014-10-15 | 青岛博睿林新材料有限公司 | 一种二次改性炉渣吸附甲醛的吸附剂 |
CN104353503A (zh) * | 2014-11-12 | 2015-02-18 | 中国海洋石油总公司 | 一种球形硅铝复合载体的制备方法 |
CN105778979A (zh) * | 2014-12-22 | 2016-07-20 | 中国石油天然气股份有限公司 | 一种降低催化裂化汽油硫含量的催化剂及其制备方法 |
CN105749867A (zh) * | 2016-04-27 | 2016-07-13 | 常州市好利莱光电科技有限公司 | 一种复合改性粉煤灰制备含铜废水处理剂的方法 |
CN106000276A (zh) * | 2016-06-30 | 2016-10-12 | 青岛惠城环保科技股份有限公司 | 一种新型硅质介孔材料及其制备方法 |
Non-Patent Citations (4)
Title |
---|
KEKA OJHA & NARAYAN C PRADHAN: ""Treated fly ash:A potential catalyst for catalytic cracking"", 《INDIAN JOURNAL OF ENGINEERING&MATERIALS SCIENCES》 * |
朱立等: ""改性粉煤灰处理含铬废水"", 《山西化工》 * |
欧阳平等: ""基于吸附的粉煤灰改性机理研究进展"", 《材料科学与工程学报》 * |
赵红娟等: ""催化裂化催化剂不同载体的孔结构及反应性能研究"", 《分子催化剂》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272764A (zh) * | 2019-06-04 | 2019-09-24 | 新奥科技发展有限公司 | 一种半焦飞灰改性剂的制备方法以及半焦飞灰的利用方法 |
Also Published As
Publication number | Publication date |
---|---|
CN107413390B (zh) | 2021-06-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Li et al. | Effects of large pore zeolite additions in the catalytic pyrolysis catalyst on the light olefins production | |
CN104340991B (zh) | 制备zsm-5沸石分子筛的方法及其产品和用途 | |
CN101269340A (zh) | 一种高硅铝比的zsm-5沸石催化剂及其制备方法和应用 | |
CN101745417B (zh) | 一种催化裂化催化剂 | |
CN104607255A (zh) | 低l酸高b酸催化裂化催化剂及其制备方法 | |
CN108452837A (zh) | 一种催化裂化催化剂 | |
CN108452830A (zh) | 一种催化裂化催化剂 | |
CN108452832A (zh) | 一种富含二级孔的含磷和稀土改性y型分子筛及其制备方法 | |
CN1245255C (zh) | 一种费托合成铁基催化剂及其制备方法 | |
Mirshafiee et al. | A green approach for template free synthesis of Beta zeolite incorporated in ZSM-5 zeolite to enhance catalytic activity in MTG reaction: Effect of seed nature and temperature | |
CN107442166A (zh) | 适于生产生物柴油的加氢催化剂及其制备方法和应用 | |
Yang et al. | Preparation of nanocrystalline ZSM-5 and its catalytic performance in fast pyrolysis of cellulose to produce aromatic hydrocarbons | |
CN104549541B (zh) | 一种重油催化裂化催化剂载体和催化剂及其制备方法 | |
Jeenpadiphat et al. | Catechol production from lignin by Al-doped mesoporous silica catalytic cracking | |
Zhang et al. | Enhanced selectivity in the conversion of glycerol to pyridine bases over HZSM-5/11 intergrowth zeolite | |
Zhang et al. | Optimizing the accessibility of zeolite Y on FCC catalyst to improve heavy oil conversion capacity | |
CN107413390A (zh) | 一种新型催化裂化催化剂载体及其制备方法 | |
CN107970978B (zh) | 一种含磷和含负载金属的mfi结构分子筛及其制备方法 | |
CN107973308B (zh) | 一种含磷的mfi结构分子筛及其制备方法 | |
CN108452831A (zh) | 一种富含二级孔的含稀土改性y型分子筛及其制备方法 | |
KR102485001B1 (ko) | 가솔린 처리 방법 | |
Amini et al. | Preparation of nanozeolite-based RFCC catalysts and evaluation of their catalytic performance in RFCC process | |
Bai et al. | Hydroisomerization of n-hexadecane over Hβ molecular sieve loading palladium bifunctional catalyst: effect of SiO2/Al2O3 molar ratios | |
CN107970984B (zh) | 一种提高汽油辛烷值桶的催化裂化助剂及其制备方法 | |
CN106622120A (zh) | 石墨烯基蛋白吸附海绵 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder | ||
CP01 | Change in the name or title of a patent holder |
Address after: No.57, Huaihe East Road, Qingdao Economic and Technological Development Zone, Shandong Province 266500 Patentee after: Qingdao Huicheng Environmental Protection Technology Group Co.,Ltd. Address before: No.57, Huaihe East Road, Qingdao Economic and Technological Development Zone, Shandong Province 266500 Patentee before: QINGDAO HUI CHENG ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |