This application is a U.S. National Stage of International application PCT/EP01/06933, filed Jun. 20, 2001.
The invention relates to an apparatus which contains a high-pressure reactor having a hydraulically controlled pressure-relief valve.
Compared with low- and medium-pressure polyethylene, high-pressure polyethylene has a higher degree of branching, a lower crystalline content, a lower melting range and lower density. In the high-pressure process, ethene is subjected to free-radical polymerization at temperatures between about 150 and 300° C. at a pressure in the range from about 1500 to 4000 bar. Oxygen or small amounts of peroxides are usually added as free-radical initiator. The corresponding reactor may be designed as a stirred-tank reactor or preferably as a flow tube. A suitable tubular reactor normally has a length of from several hundred to a few thousand meters and is surrounded on the outside by a heating or cooling jacket. Owing to the high internal pressure in the reactor, the walls of the tubular reactor, which are made of metal, typically have a thickness in the order of a few cm.
Technical problems in the high-pressure process are explained in “Chem-Ing.-Tech. 67 (1995) No. 7, pages 862 to 864, Verlag VCH-Verlagsgesellschaft GmbH Weinheim”. Thus, it is stated that ethene decomposes rapidly in an explosive manner under certain temperature and pressure conditions to give soot, methane and hydrogen. This undesired reaction occurs repeatedly, in particular in the high-pressure polymerization of ethene. The drastic increase in pressure and temperature associated therewith represents a considerable potential risk for the operational safety of the production plants.
One possible solution for preventing a drastic increase in pressure and temperature of this type consists in installing rupture discs in the tubular reactor. However, the disadvantage of rupture discs of this type is that, at the high pressures prevailing, they do not react to relatively small pressure variations—this means that rupture discs may burst in an undesired manner within the range of the usual operating pressures. A further significant disadvantage of rupture discs is that they do not respond to increases in temperature. As an alternative to rupture discs, it is possible to employ so-called emergency T-valves (pressure-relief valves). Pressure-relief valves of this type are opened or closed by a hydraulic control mechanism. Since such a hydraulic control mechanism is relatively slow to react, correspondingly low opening speeds result for the corresponding pressure-relief valves.
The object of the present invention is thus to provide a high-pressure reactor in which the occurrence of sudden pressure or temperature increases causes particularly rapid relief (decompression or temperature reduction). The relief of the reactor should be reliable and take place at a sufficiently high speed.
This object is then achieved by an apparatus containing
The high-pressure reactor is generally designed as a tubular reactor, but can also be designed as a high-pressure autoclave. The high-pressure reactor is usually employed for the production of ethylene polymers. Suitable measurement devices for the determination of temperature or pressure are commercially available sensors. The movable piston mass is taken to mean the part of the hydraulic cylinder which is moved by the hydraulic fluid during closing or opening of the pressure-relief valve. The movable piston mass usually comprises the hydraulic piston and a corresponding valve spindle. The connecting lines provided for conveying hydraulic fluid are preferably designed as tubes.
The main advantage of the present invention is that pressure jumps in the high-pressure reactor can be relieved extremely quickly. The magnitude of the corresponding opening operation for the pressure-relief valve is only about 50 ms. In contrast to known pressure-relief systems, this is sufficiently fast for reliable relief (decompression or temperature reduction) of the high-pressure reactor. A further essential advantage of the invention is that the pressure relief can be initiated both by pressure and temperature jumps.
Fast and reliable relief of the reactor is also achieved, inter alia, through the pressure-relief valves having a seat cross section which is generally at least about 350 mm2 per m3 of reactor volume. In the temperature maxima of the reactor, wherever possible up to 800 mm2 of seat cross section per m3 of reactor volume should be implemented.
The internal volume of the high-pressure reactor is usually from 1 to 15 m3. The preferred internal pressure of the high-pressure reactor is from 2000 to 3500 bar.
At least one connecting line between the hydraulic control unit and the hydraulic system usually has on average an internal diameter of from 20 to 50 mm—preferably, all connecting lines situated between the hydraulic control unit and the hydraulic system have on average an internal diameter of from 20 to 50 mm. The at least one connecting line generally has an internal pressure of from 150 to 250 bar—usually, all connecting lines situated between the hydraulic control unit and the hydraulic system have an internal pressure of from 150 to 250 bar. In a preferred embodiment of the invention, two connecting lines provided for conveying hydraulic fluid are arranged between the hydraulic control unit and the hydraulic system. One of these connecting lines carries hydraulic fluid to the hydraulic control unit, the corresponding other from the hydraulic control unit to the hydraulic system.
The movable piston mass preferably weighs from 15 to 50 kg.
In a preferred embodiment of the invention, a connecting line, or the connecting line through which hydraulic fluid is conveyed from the hydraulic system in the direction of the hydraulic control unit during the opening of the pressure-relief valve, is fitted with a one-way restrictor. The one-way restrictor is able to eliminate the disadvantage that the corresponding valve seat fittings are damaged during the closing operation of the pressure-relief valve. The installation of the one-way restrictor enables the speed of the closing operation to be adjusted—in general, a closing time of about 2 s proves successful. The one-way restrictor thus enables rapid opening and delayed closing of the pressure-relief valve, promoting long service lives of the “pressure-relief system”.
In general, one or more valves of the hydraulic control unit are designed as sliding valves with ball seat actuation.
The pressure-relief valve is preferably opened by moving the movable piston mass either toward or preferably away from the pressure-relief valve.
In the attached drawing,
The outlet 14 of the pressure-relief valve 11 is provided with a high-level pot 15 for the separation of solid (for example polyethylene). The connecting lines 8, 12 have an internal diameter of from 10 to 80 mm, preferably from 20 to 50 mm. The pressure therein is from 100 to 500 bar, preferably from 150 to 250 bar.
Number | Date | Country | Kind |
---|---|---|---|
100 31 586 | Jun 2000 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/EP01/06933 | 6/20/2001 | WO | 00 | 6/4/2003 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO02/01308 | 1/3/2002 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
4550747 | Woodworth et al. | Nov 1985 | A |
5026527 | Krijgsman | Jun 1991 | A |
5054517 | Liesenhoff et al. | Oct 1991 | A |
5149507 | Ellis, Jr. | Sep 1992 | A |
5533551 | Grancher | Jul 1996 | A |
Number | Date | Country |
---|---|---|
0 540 915 | May 1993 | EP |
Number | Date | Country | |
---|---|---|---|
20040013588 A1 | Jan 2004 | US |