Chemistry of hydrocarbon compounds – Unsaturated compound synthesis – By c content reduction – e.g. – cracking – etc.
Reexamination Certificate
1999-12-06
2001-08-07
Griffin, Walter D. (Department: 1764)
Chemistry of hydrocarbon compounds
Unsaturated compound synthesis
By c content reduction, e.g., cracking, etc.
C585S648000, C585S650000, C585S921000, C208S130000
Reexamination Certificate
active
06271431
ABSTRACT:
The invention relates to a process for thermal pyrolysis of a feedstock that contains at least 80% ethane. The ethylene that is obtained is used in particular for the synthesis of polyethylene.
Ethylene is currently produced by steam-cracking the ethane, which is a process that is broadly described in the literature. Taking into consideration the limitations of the mechanical behavior, in terms of temperature, of the metallic materials that are currently used, the conversion of the ethane is less than 70%. There is therefore at least 30% of ethane that is recycled and that represents a significant cost because this ethane is to be compressed, cooled and separated from the effluent.
A recent so-called radiant-tube technology in ceramic furnaces that is described by the applicant (EP-B-542597, EP-B-666104) makes it possible to obtain an effluent with a high conversion of the feedstock, for example up to 100% if it is desired. Whereby the recycling of the unconverted feedstock is greatly reduced and even almost zero, it is possible either to reduce the size and therefore the cost of the separation section for the new installations or to increase productivity of olefins with the same separation section for an existing unit. Thus, according to the patent of the applicant EP-B-542597, the pyrolysis of the naphtha in a furnace that comprises electric resistors that are insulated from direct contact with hydrocarbons by porous sheaths that contain a gas is described, and an effluent with an ethylene yield by weight of 39.6% and 16.4% of propylene is produced.
According to another patent of the applicant, EP-B-664104, a reactor with pyrolysis by heat exchange means, at least some of which contain at least one tube that is formed by at least one jacket that is connected to a gas supply means or heat exchange gas mixture, is described. These heat exchange means that are fed by gas communicate with gas burners. The process that is employed describes the pyrolysis of a butane-isobutane mixture that is diluted in nitrogen and that makes it possible to obtain 9 mol % of a mixture of ethylene and acetylene that contains 37 mol % of acetylene.
To increase the selectivity toward the production of olefins, several previous studies quickly led to a very high-temperature heating of the furnaces and to decreasing the dwell time of the feedstock in the reaction zone. Unlike the teaching of these patents, it was noted that by operating at the lowest possible reaction temperature and with the longest possible dwell time in the reaction zone, it was possible to increase the conversion of the feedstock while keeping the ethylene selectivity at a very correct level, for example greater than 75%. None of these cited patents teach or suggest pyrolyzing an ethane feedstock in the presence of water vapor with long dwell times, greater than 1 second. This is therefore one of the objects of the invention.
Another object is to produce ethylene with a minimum of impurities and in particular acetylene. Another object is to produce ethylene with the highest selectivity possible for a given ethane conversion rate and more particularly in the range of high conversion levels.
More particularly, the invention relates to a process for thermal pyrolysis of a feedstock that contains at least 80% ethane by weight in a reaction zone that comprises a heating zone and a cooling zone behind the heating zone, characterized in that the operation is performed in the presence of water vapor under the following conditions:
temperature at the outlet of the heating zone of between 880° C. and 960° C.,
dwell time of the feedstock in the heating zone of between 1005 milliseconds and 3000 milliseconds (ms), in particular greater than 1020 milliseconds;
whereby the temperature and the dwell time are selected so that the conversion that is obtained of the feedstock is at least equal to 80%,
and an effluent that contains ethylene for the most part is recovered.
It is preferably possible to proceed at a temperature at the outlet of the heating zone of between 890° C. and 950° C., most often between 910° C. and 930° C. and with a dwell time of the feedstock of 1050 milliseconds to 2800 milliseconds, most often 1200 milliseconds to 2000 milliseconds to convert at least 85% of the feedstock and most often at least 88%.
It was observed more particularly that it was possible to proceed at the lowest possible reaction temperature and with the longest possible dwell time of the feedstock in the heating zone that are compatible with the desired conversion rate.
Under these conditions, the recycling rates of unconverted feedstock in the pyrolysis reactor are reduced by operating under conditions that make it possible to convert the feedstock as much as possible, and the size of the equipment that is downstream from the separation is reduced since the ethylene selectivity is maximized. The process is therefore more economical.
The conversion reaction of the ethane according to the invention into ethylene can be implemented in a reactor in which the heating zone comprises heating means that are placed approximately perpendicular to the direction of the flow of the feedstock and the effluent.
This heating zone can comprise electric resistors that are encased in ceramic sheaths that are approximately perpendicular to the flow. The latter can contain at least one cover gas that can be water vapor or nitrogen. In patent EP-B 542597 that is incorporated as a reference, the applicant described an embodiment of the reactor that can be used for the implementation of the invention. According to a variant, the heating zone can comprise, as it is described in the patent of the applicant EP-B-666104 that is incorporated as a reference, a number of heat exchange means that are approximately perpendicular to the flow and that each comprise a tube that is formed by at least one jacket that is connected to a supply means of gas or a heat exchange gas mixture that is suitable for exchanging heat with the feedstock and/or the effluent that circulates outside of said heat exchange means a n d that comprises at least one evacuation means outside of the reactor of said gas or gas mixture that has exchanged heat with the feedstock and/or the effluent.
The feedstock, after having been preheated between 700° C. and 750° C., for example, can be heated in an increasing manner, for example an approximately linear manner, to the temperature that is selected at the end of the heating reactor.
According to a characteristic of the invention, it is possible to heat the heating zone according to a temperature gradient that is generally between 40° C./s and 350° C./s and preferably between 80° C./s and 150° C./s. As has been indicated, this gradient can be kept approximately constant during the heating period or even increases as a function of time. The heating zone preferably contains a number of rows in which the feedstock circulates and that comprise the heating elements that are perpendicular to them. These rows are separated by partitions that make it possible to increase the exchange surface. The form of these partitions can conform in shape to that of the heating elements. In a horizontal plane, each row preferably contains a single heating element between two adjacent partitions. An embodiment is described in Patent EP-B-666104 that is incorporated as a reference according to FIG. 1 B of this patent.
Another embodiment of the reactor is described in the patent of the applicant EP-A-781828 that is incorporated as a reference, in which at least one row can be dedicated to a decoking stage by the water vapor during the operation of the unit under endothermic conditions at a temperature that is compatible with that of the process according to the invention, while at least one row is intended for the steam-cracking of the feedstock.
The dwell time that is generally selected, the longest possible that is compatible with the lowest temperature of the isoconversion reactor, is linked to the reaction volume. To obtain it, for a given production of ethylene, it is possible to increase
Burzynski Jean-Pierre
Busson Christian
Delhomme Henri
Nougier Luc
Griffin Walter D.
Institut Francais du Pe'trole
Millen White Zelano & Branigan P.C.
Nguyen Tam M.
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