文献翻译-反应釜用机械密封设计Word文档格式.doc

1、 300 liter vertical reactor, stirring shaft inserted from the top, single-bearing; Maximum working pressure; 25kgf/cm;Temperature: room temperature 15O Stirring speed: 12O 150rpm;Medium: dilute ammonia + dehydroacetate powder + solvent Biochemistry;Shaft diameter: 30mm, diameter length ratio: 1:50;A

2、xial space: Kamaguchi coupling flange to the back side while the height is about 293mm;Operation: Intermittent operation, stopping frequently to open;Leakage: 3ml / h;Life: 8000 h （one year）. Third, technical analysis and design According to the conditions and requirements of a given point of view,

3、the mechanical seal is a very harsh operating conditions. The main problems involved:1. Top loading autoclave technical problems with the nature of the mechanical seal pump mechanical seal completely different, because it is in the vapor space （only the material is liquid when the tank is full）, sea

4、l prone to dry run.2. As the medium is the chemical reaction within the reactor, pressure, temperature, material and shape change are always asked, in the stress cycle and the role of thermal cycles, the seal faces deform easily. 3. Mechanical seal used at room temperature, due to the friction surfa

5、ce of the heating and sealing of the mixing heat will seal the room temperature rise. When used at high temperatures, due to heat conduction within the tank, the temperature will further rise, causing friction surface of the liquid film evaporation, resulting in dry run, and to promote corrosion, ac

6、celerated aging auxiliary ring, resulting in deterioration in the short term sealing performance. 4. Stirring shaft inserted from the top vertical reactor, its diameter longer than large. It is a single support, the amount of its inevitable swing higher. 5. In the reaction process, the mixer blades

7、and fluid material generated by relative motion between the vortex, must be caused by mixing shaft vibration. 6. May also occur for the following reasons axis traverse:（1） uneven or liquid feed is too low;（2） formation did not control the reactants, viscosity increases;（3） sudden changes in speed mi

8、xer;（4） thermal expansion or pressure and temperature fluctuate. 7. Because the top of the reactor very easy to install seal. Kettle mechanical seal in the structure must be easy to install and removal. In the past, mechanical seal failure resulting in performance, many of them are caused by poor in

9、stallation of the reactor because the existing parts of mechanical seal to the reactor need to install one by one, we should ensure that its accuracy is difficult. According to the conditions given by the user and the technical analysis to determine the following basic design:1. Higher use of safety

10、 barrier double end mechanical seal, to ensure the reactor sealed. 2. Sealed from the outside to enter the clean room suitable for the lubrication of cooling liquid resistance sealed, and set the cooling water jacket, to improve the sealing of the operating conditions 3. The structure of the sealing

11、 device, additional bearings to reduce shaft deflection and a rocky ledge. 4. Consider the ease of installation and removal, and economic factors. 4, structural design features According to the design of mechanical seal design, the friction pair material for the surfacing alloy carbon Graphite, supp

12、orting ring material: NBR a 4O. Specific technical measures;1. Consider the pressure fluctuations in the design of the seal by 30kgf/cm. Side sealing surface of the upper atmospheric pressure to bear large, so designed as balanced, 30%, static method supports dual-ring seal 0-ring to reduce the stat

13、ic part of the deformation. Medium within the lower part of the lateral side of the sealing surface pressure is small, it is designed to be non-balanced. It is worth noting that this side of the seal may seem easy, in fact, not. If not handled properly cause leaks, pollution vessel will be within th

14、e material, resulting in product failure, we must give our full attention. Under static compression ring does not use the traditional structure, but with good use of the following floating-mounted so that the end is always the best fit to maintain the state. 2. Installation of a shorter axial dimens

15、ion structure, because the seal and spring seat sharing a drive. With a sleeve on the keyway and fixing screw to drive the drive seat, sturdy and reliable 3. The structure of the seal bearing added to improve the dynamic stability of the mixing shaft （measured at the tank flange runout of the shaft

16、0.05mm）. Mechanical seal from the bearing mounted close to the place, thus enhancing the sealing operation stability. 4. Offices in the sealed chamber cooling water jacket to reduce heat from the reactor body to pass chamber. 5. Introduced to the sealed chamber from an external sealing liquid, on th

17、e mechanical seal lubrication, cooling and block letters. 6. The seal structure has a fast and accurate installation and removal of benefits. The seal as an integrated whole, can be pre-assembled, and tested, and then loaded on to the kettle, do not need to re-adjust. If the seal fails, the entire s

18、eal can be removed, the pre-assembly, debugging can be a good backup seal fitted. Therefore, the installation, maintenance and replacement is very convenient, stopping at the same time greatly reducing the time, with obvious economic Benefits. 5, sealing liquid system For the reactor with double mec

19、hanical seal, the sealing performance and stability to make long working life, the key is to use proper sealing liquid system. On the basic requirements of sealing liquid system is to ensure the safe operation of seal, namely:1. Under a certain pressure, to send the seal on the sealing liquid to mai

20、ntain the liquid film between the friction surface and form a barrier between the material and the atmosphere to ensure that materials not leak fluid. 2. Closed loop liquid circulation should be sufficient to take away the heat generated by friction surface and by stirring shaft or container to avoi

21、d the conduction of heat to the sealing device. 3. Ensure that the Kettle is always in proper operating condition. The design of the sealing liquid pressure control system uses both methods, that is, the top pick out of a kettle body 1-inch pipeline to a pressure tank top. Pressure tank installed in

22、 the sealed room above the 2 m Department. Sealing liquid seal chamber exit at the highest point of the water jacket, thermal siphon effect to achieve the purpose of the cooling cycle. The volume of pressure tank 2O liters, made of stainless steel. The peripheral cooling jacket, heat transfer area o

23、f 0.02 square meters, to prevent the sealing liquid temperature oxidation and deterioration. Pressure tank to the highest pressure 30kgf / c . Set obituary. Attachments are used in pressure gauge, liquid level meter, and thermometers, exhaust valve and drain valve, liquid filling the mouth and so on

24、. Sealing liquid with dilute glycerol （glycerin, and soft water of 50%）, once every three months to replace. Because the system uses thermal siphon method, a simple economy, the pressure changes inside the reactor to follow, and can ensure that the seal fluid pressure within the pressure slightly hi

25、gher than the kettle. VI Conclusion Chemical, pharmaceutical production in stirred tank reactor, the leakage demanding. If excessive leakage will result in product failure or shutdown, so the need for effective and reliable seal device. Practice shows that the mechanical seal to meet their requireme

26、nts. This article describes the reaction vessel with a mechanical seal for a chemical plant in Anhui design. Since the on-site installation of the seal after the sealing performance and stability, leakage is extremely small, life nearly two years, still continue to use.反应釜用机械密封设计机电部通用机械研究所 陈德才一、前言搅拌

27、式反应釜是化工、制药生产中的关键设备之一， 其运行效率和可靠性很大程度上取决于轴封装置的优劣 尤其是高压高温反应釜的轴封是当前需要专门解决的问题。国内已定型的标准型釜用机械密封产品有201、202、203、204，205、206型， 其使用压力为116kgfcm ， 轴径为30 ll0mm。近年来， 随着石化、制药工业的发展， 搅拌反应釜的反应压力、温度随之增高， 并向着高性能方向发展。同时从防止污染以及安全、节能等角度出发，对轴封装置的可靠性、寿命、泄漏量和经济性等方面的要求也越来越高。因此，现有的标准型釜用机械密封产品已不能完全满足其要求， 达就需要根据使用工况进行专门设计。本文就一种高温

28、高压反应釜用机械密封的设计作一概要的介绍。二、用户给定条件装置：300立升立式反应釜， 搅拌轴从顶部插人， 单支承；最高工作压力；25kgfcm ；温度：室温15O搅拌速度：12O150rpm;介质：稀氨水+脱氢醋酸粉料+生物化学溶剂；轴径：30mm， 径长比： 1：50；轴向空间: 釜口法兰至联轴节背端而高度约为293mm;操作方式： 间歇操作， 开停频繁;泄漏量:3mlh;寿命: 8000 h （一年）。三、技术分析和设计思想根据给定的条件和要求来看， 该机械密封的运转条件是相当恶劣的。所涉及的主要问题是:1顶装釜用机械密封的技术问题性质完全不同于泵用机械密封， 因为它是处于气相空间中（只有物料为满釜时才是液相），密封易出现“干运转”。2 由于介质是在釜内进行化学反应， 压力、温度、物料的形态等都是随时问而变化的，