CN103212431A - 加氢裂化催化剂以及制备液态烃的方法 - Google Patents
加氢裂化催化剂以及制备液态烃的方法 Download PDFInfo
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Abstract
本申请涉及一种加氢裂化催化剂以及制备液态烃的方法。一种包括结晶硅铝酸盐、氧化铝-氧化硼和周期表第VIII族贵金属的催化剂。这是一种能获得高裂化活性、高中间馏分油收率和低倾点瓦斯油产物的链烷烃加氢裂化催化剂。
Description
本申请是2005年3月10日提交的申请号为200580010484.7的专利申请“加氢裂化催化剂以及制备液态烃的方法”的分案申请。
发明领域
本发明涉及一种用于在氢气的存在下从链烷烃制备液态烃的催化剂以及利用该催化剂制备液态烃的方法。
发明背景
近年来，对硫和芳烃含量低的清洁液体燃料的需求迅速增加。为了响应所述的需求，燃料油生产商已研究了各种生产清洁燃料的方法。在这些方法当中，被认为最具有前景的方法是将链烷烃如石蜡在催化剂的存在下进行加氢裂化的方法。
在链烷烃加氢裂化工艺中，重要的是以更高的收率生产有用的中间馏分油，从而提高该工艺的经济效率。另外，所得瓦斯油还必需具有低倾点。也就是说，开发出能提高加氢裂化工艺的裂化活性和中间馏分油收率并使该工艺能生产低倾点瓦斯油的高效加氢裂化催化剂是提高该工艺经济效率的关键。
减压瓦斯油的加氢裂化已经商业化并且是创立了几十年的技术。但是，由于链烷烃的反应性与减压瓦斯油的反应性之间的差异是如此显著，以至于难以将用于减压瓦斯油的催化剂原样用于链烷烃的加氢裂化反应，因此不断加大研究和开发力度以开发出能用于链烷烃的高效催化剂。只有很少的一些有关此类催化剂的专利和报道。例如，下面的专利文献1公开了一种包括负载于含硅铝氧化物载体内的铂的催化剂。在非专利文献2研究的一个实施例中使用包括负载于结晶硅铝酸盐(沸石)内的铂的催化剂来实施链烷烃加氢裂化反应。
但是，结晶硅铝酸盐催化剂虽然可使裂化活性达到令人满意的高水平，但不利的是中间馏分油的收率低且所得瓦斯油不能获得足够的倾点。另一方面，无定形固体酸催化剂(典型例子是硅铝催化剂)可使中间馏分油的收率和所得瓦斯油的倾点达到令人满意的高水平，但裂化活性低。也就是说，迄今还没有开发出一种能满足高的裂化活性和中间馏分油收率同时所得瓦斯油倾点低的催化剂，由此严重阻碍了链烷烃加氢裂化工艺经济效率的提高。
(1)专利文献1：日本专利公开号6-41549
(2)非专利文献2：“沸石”(第6卷，334-348页，1986)
发明内容
本发明的目的是提供一种用于链烷烃加氢裂化的新型催化剂，所述催化剂可同时满足裂化活性和中间馏分油收率较高以及所得瓦斯油倾点较低，由此提高加氢裂化过程的产率。
本发明人进行了深入研究，结果发现用一种包括结晶硅铝酸盐和氧化铝-氧化硼的组合的催化剂可解决上述问题，据此而完成了本发明。
即，本发明涉及一种链烷烃加氢裂化催化剂，包括结晶硅铝酸盐、氧化铝-氧化硼和周期表第VIII族贵金属。
本发明还涉及一种其中结晶硅铝酸盐平均粒径为0.5μm或更小的上述催化剂。
本发明还涉及一种使用上述催化剂将链烷烃进行加氢裂化来制备液态烃的方法。
下面将更详细地描述本发明。
本文所用的术语“硅铝酸盐”表示由三种元素即铝、硅和氧所构成的金属氧化物。尽管可共存另外的金属元素，但其量应为不至影响到本发明达到良好效果的程度，该氧化物形式的金属元素的量为氧化铝和氧化硅总量的5质量％或更少且优选3质量％或更少。可共存的金属元素的例子是钛、镧、锰、镓和锌。优选钛和镧。
硅铝酸盐的结晶度可以用所有Al原子中四面体配位的Al原子的比率来估算，所述的比率可通过固体27Al NMR波谱法测定。本发明中所用的术语“结晶硅铝酸盐”表示四面体配位的Al原子比率为50％或更高的硅铝酸盐。任何结晶硅铝酸盐都可用于本发明，只要四面体配位的Al原子比率为50％或更高即可。但是优选使用包含70％或更高的四面体配位的Al原子的结晶硅铝酸盐，更优选使用含80％或更高的四面体配位的Al原子的结晶硅铝酸盐。
适用于本发明的结晶硅铝酸盐是所谓的沸石。优选Y-或USY-型沸石、β-型沸石、丝光沸石和ZSM-5，最优选USY-型沸石。如果需要，可使用两或多种类型的结晶硅铝酸盐。
对本发明所用结晶硅铝酸盐的平均粒径没有特另限制。但是，优选平均粒径为1.0μm或更小，特另优选0.5μm或更小。
本发明的加氢裂化催化剂的特征在于它包括结晶硅铝酸盐和氧化铝-氧化硼。对氧化铝-氧化硼中氧化铝与氧化硼之含量比没有特别的限制。但是，氧化铝与氧化硼之比通常优选为30-99质量％：70-1质量％、更优选50-95质量％：50-5质量％、且最优选70-90质量％：30-10质量％。
对催化剂中结晶硅铝酸盐与氧化铝-氧化硼的质量比没有特别的限制。但是所述的质量比通常优选为0.001-2.000、更优选0.010-1.500、且最优选0.015-0.200。
可不使用粘结剂将催化剂模制成所需形状。但是，如果需要的话，可使用粘结剂。对粘结剂没有特别的限制。但是，优选的粘结剂是氧化铝、氧化硅、氧化硅-氧化铝、二氧化钛和氧化镁，且最优选的是氧化铝。对整个模制催化剂中粘结剂的百分率没有特别的限制。但是，该百分率通常为5-99质量％，优选20-99质量％。
本发明的催化剂必须含有周期表第VIII族贵金属作为活性组分。当用非周期表第VIII族金属的金属作为活性剂时，用含该金属的催化剂进行加氢裂化得到的中间馏分油的收率会极度下降，从而不能实现本发明的目的。
周期表第VIII族贵金属的具体例子包括钴、镍、铑、钯、铱和铂。最优选的是钯和铂。可通过已知方法如浸渍法或离子交换法将这些金属负载于上述模制催化剂上来制备本发明催化剂。
如果需要，可以将两或多种贵金属组合负载。例如，同时负载铂和钯。对贵金属的负载量没有特别的限制。基于催化剂的总质量计，负载量通常为0.02-2质量％。
在本发明中，本文所用的术语“链烷烃”表示链烷烃分子的含量为70摩尔％或更高的烃。对烃分子的碳原子数没有特别的限制。但是，通常使用有10-100个碳原子的链烷烃。本发明催化剂对具有20或更多个碳原子的链烷烃即所谓“石蜡”的加氢裂化反应特别有效。
对将成为加氢裂化过程原料的链烷烃的生产方法没有特别的限制。因此，本发明的催化剂可应用于各种链烷烃，如石油基或合成链烷烃。但是，特别优选的链烷烃是通过费-托合成过程生产的所谓FT石蜡。
本发明催化剂可用于常规固定床反应器装置。反应条件是反应温度为200-500℃，氢压为0.5至12MPa，链烷烃原料的LHSV(液时空速)为0.1-10/h。优选的条件是反应温度为250-400℃，氢压为2.0-8.0MPa，链烷烃原料的LIISV(液时空速)为0.3-5.0/h。
工业应用
将包括结晶硅铝酸盐、氧化铝-氧化硼和周期表第VIII族贵金属的本发明催化剂用于链烷烃加氢裂化反应时，可同时获得高的裂化活性和中间馏分油收率以及所得液态烃的倾点低。
实施本发明的最佳方式
下面将参照实施例和对比例更详细地描述本发明，但本发明不受限于此。
(实施例1)
将包括30g平均粒径约0.4μm的USY沸石和970g氧化铝-氧化硼的尺寸为1/16英寸(约1.6mm)的柱状载体用含有二氯四氨合铂(II)的水溶液浸渍，使铂元素的量为载体的0.8质量％。将该载体在120℃下干燥3小时，然后在500℃下焙烧1小时，由此制得催化剂。
将所制备的催化剂(200ml)填充入固定床流动反应器中并用来对链烷烃进行加氢裂化。本文所用的原料是链烷烃含量为95％且碳数分布为20至80的FT石蜡。氢压为3MPa，原料的LHSV为2.0/h。将沸点为360℃或更低的级分定义为“裂化产物”。测定能获得裂化产物为原料量80质量％的反应温度。还测定沸点为145℃-360℃的中间馏分油的收率，以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
(实施例2)
将30g平均粒径约为0.4μm的USY沸石、570g氧化铝-氧化硼粉末和400g用作粘结剂的氧化铝进行模制，由此得到尺寸为1/16英寸(约1.6mm)的柱状载体。按照与实施例1相同的方式将铂负载到载体内，使铂的量为载体的0.8质量％。将载体在120℃下干燥3小时，然后在500℃下焙烧1小、时，由此制得催化剂。
按照与实施例1相同的方式用该催化剂进行加氢裂化反应，以便测定能得到裂化产物为原料量80质量％的反应温度，测定沸点为145℃-360℃的中间馏分油的收率以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
(实施例3)
按照与实施例1相同的方法进行催化剂的制备和加氢裂化，所不同的是用平均粒径为0.8μm的USY型沸石，这样来测定能得到裂化产物为原料量80质量％的反应温度，测定沸点为145℃-360℃的中间馏分油的收率以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
(对比例1)
按照与实施例1相同的方法进行催化剂的制备和加氢裂化，所不同的是用氧化铝代替氧化铝-氧化硼，这样来测定能得到裂化产物为原料量80质量％的反应温度，测定沸点为145℃-360℃的中间馏分油的收率以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
(对比例2)
按照与实施例1相同的方法进行催化剂的制备和加氢裂化，所不同的是不使用USY-型沸石，这样来测定能得到裂化产物为原料量80质量％的反应温度，测定沸点为145℃-360℃的中间馏分油的收率以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
(对比例3)
按照与实施例1相同的方法进行催化剂的制备和加氢裂化，所不同的是载体负载有基于载体计5质量％的镍和基于载体计15质量％的钨来代替铂，这样来测定能得到裂化产物为原料量80质量％的反应温度，测定沸点为145℃-360℃的中间馏分油的收率以及所得沸点为260℃-360℃的瓦斯油的倾点。结果示于下表1中。
从表1所示的结果可明显看出，结晶硅铝酸盐和氧化铝-氧化硼的组合可同时满足高裂化活性、高中间馏分油收率和所得瓦斯油的倾点低。此外，还明显看出，周期表第VIII族贵金属作为活性金属是有效的。
表1
Claims (6)
1.一种链烷烃加氢裂化催化剂，所述链烷烃加氢裂化催化剂由沸石、氧化铝-氧化硼和周期表第Ⅷ族贵金属组成。
2.权利要求1所述的链烷烃加氢裂化催化剂，其中沸石的平均粒径为1.0μm或更小。
3.权利要求1所述的链烷烃加氢裂化催化剂，其中沸石的平均粒径为0.5μm或更小。
4.一种制备液态烃的方法，包括用催化剂加氢裂化链烷烃，所述催化剂由沸石、氧化铝-氧化硼和周期表第Ⅷ族贵金属组成。
5.权利要求4的制备液态烃的方法，其中沸石的平均粒径为1.0μm或更小。
6.权利要求4的制备液态烃的方法，其中沸石的平均粒径为0.5μm或更小。
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| AU2005225266A1 (en) | 2005-10-06 |
| US7700818B2 (en) | 2010-04-20 |
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Application publication date: 20130724 |