• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1. A DEVICE FOR SULPHATING ORGANIC REAGENT, comprising a vertically installed housing with a nozzle, a product withdrawal, a pipe for supplying a gaseous sulphating agent, a liquid organic reagent and a cooled product, and a heat exchanger connected by pipelines with a nozzle for withdrawing the product and the pipe, feeding the cooled product, characterized by that, in order to prevent charring and increasing the yield of the product, it is equipped with a venturi pipe connected to the upper part of the body with a suanicis an ejection and expansion outlet part, the liquid organic reagent supply pipe is installed inside the supply pipe of the gaseous sulphating agent along its axis and is equipped at the end with an injection unit located at the subparts of the Venturi pipe, the output part of which is connected to the housing in which it is terminally mounted chilled product supply pipe with an injection unit located at the outlet of the Venturi pipe. 2. The device according to claim 1, characterized in that it is provided with an air supply pipe, which encloses the liquid organic reagent supply pipe and has an air supply nozzle installed upstream of the liquid organic reagent injection unit in the air supply direction i, the output end of the air supply pipe protruding for the liquid organic reagent injection unit. 3. The device according to claim 1, characterized in that it is provided with a unit for supplying cooled product to the outlet part of the Venturi tube. 4. The device according to claim 1, wherein it is provided with a gas supply pipe for the sulphating agent installed at an angle to the axis of the gas supply pipe of the sulphurized agent, in which the means for smoothing the flow are mounted. 5. The device according to claim 1, characterized in that it is provided with an additional liquid organic reagent supply pipe connected to a pipe connecting the heat exchanger with the lower end of the cooled product supply pipe.
    公开号:SU1148558A3
    申请号:SU792790956
    申请日:1979-06-25
    公开日:1985-03-30
    发明作者:Брукс Бартон；Дж.Брукс Ричард
    申请人:Дзе Кемитон Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to an apparatus for the sulfonation of an organic reagent with the aid of a sulfonating agent containing sulfur trioxide.
    A device for sulfonation of an organic reagent is known, comprising a vertically mounted housing with a product outlet pipe, a sulphating gas supply pipe, a liquid organic reactant and a cooled product, and a heat exchanger, connected to the product outlet pipe and the cooled product supply pipe. The device operates as a film reactor of the p-type J.
    The disadvantages of this device are the complexity of the distribution unit of the liquid organic reagent in the form of a film on the walls of the case, the possibility of burning the product and. the need to periodically clean the walls of the casing to remove resinous or resinous material that impairs heat transfer through the casing of the device.
    In addition, in the known device there is a significant air flow to obtain a gaseous sulphating agent, which leads to an increase in the size of auxiliary equipment (dryers for: air, gas separators, scrubbers, pipelines), as well as to significant energy costs.
    The purpose of the invention is the prevention of charring and the increase in product yield.
    The goal is achieved by the fact that a device for: sulphurization of organic reagent, containing a vertically installed housing with a product outlet, a pipe for supplying a sulphating gaseous agent, a liquid organic reagent and a cooled product. And a heat exchanger connected by pipelines to the product outlet and the pipe the supply of the cooled product according to the invention is provided with a venturi tube connected to the upper part of the body with a suzhaktsev the inlet part, the neck and the expanding output part, with the supply pipe of liquid organic reagent installed inside the pipe supplying a gaseous sulphating agent along its axis and provided with an end at the end
    injection located at the supply part of the Venturi tube, the output part of which is connected to the case in which the cooled product supply pipe is concentrically mounted with the outlet unit located at the outlet part of the Venturi pipe.
    In addition, the device can be equipped with an air supply pipe, encompassing the liquid organic reagent supply pipe and having an air supply nozzle, installed 1 to the liquid organic reagent injection unit along an air supply, the output end of the air supply coarsement extending beyond the liquid organic reagent injection unit .
    The device can be equipped with a unit for supplying cooled product to the outlet part of the Venturi pipe.
    In this case, the device is equipped with a sulfuruk gaseous agent supply nozzle installed at an angle to the axis of the pipe for supplying the gaseous sulfonating agent, in which the means for is mounted. smoothing flow.
    The device may also be provided with an additional liquid organic reagent supply pipe connected to a pipeline connecting the heat exchanger to the lower end of the cooled product supply pipe.
    Such a device can significantly increase the concentration of sulfur trioxide (for example, up to 7-10%) in air, since the reaction mainly occurs in the quenching zone (rapid cooling), where the possibility of charring the product is less, which leads to a significant increase product yield without reducing its quality;
    At 1, the device is shown schematically in section; in fig. 2 - technological scheme of the device; in fig. 3 - pipe for supplying liquid organic reagent (embodiment).
    The device for sulphurization of liquid organic reagent comprises a vertically installed body 1 with a pipe 2 for withdrawing the product, a pipe 3 for supplying a gaseous sulphurizing agent, a pipe 4 for supplying a liquid organic reagent and a pipe 5 for feeding a cooled product. The device is equipped with a venturi tube connected to the upper part of the housing 1 with a tapered supply part 6, a throat 7 and an expansion part with an output part 8. The pipe 4 for supplying liquid organic reagent is installed inside the pipe 3 for supplying a gaseous sulfonating agent along its axis the injection unit 9, which is located at the inlet part 6 of the Venturi tube, the output part 8 of which is connected to the casing 1. The cooled product supply pipe 5 is concentrically mounted in the housing 1 and equipped with an injection unit 10, the gas supply pipe 3 different sul fyruyuschego agent connected to the lead-in part 6 of the Venturi tube and mounted coaxially therein. The length of pipe 3 is about 10 times its diameter, which ensures smoothing of the flow. Means for smoothing the flow (not shown) and a supply pipe 11 for supplying a gaseous sulphurizing agent installed at an angle to the axis of the pipe 3 for supplying sul gas 4 with a 1 agent can also be mounted in the pipe 3. In the pipe 3 there are holes 12 and 13 for accommodating measuring means temperature and pressure. The device is also equipped with a heat exchanger 14, connected by pipeline 15, pump 16, pipeline 17, with parator-cycle 18, pipeline 19 with pipe 2 of the product outlet. The heat exchanger 14 is also connected to the pipeline. 20. With the lower end of the cooled product supply pipe 5, the Separator-cyclone 1B is connected to the atmosphere by a pipe 21. The pipeline 15 departs, the pipeline 22, which is connected to the separator-cyclone 18 by the pipeline 23, the device can be equipped with a cooling supply assembly 24 to the outlet part 8 of the Venturi tube, the feeding assembly 24 is made with a slit and with: one with the pipeline 20 heat exchanger 14 with the lower end of the chilled product supply pipe 5. The injection unit 9 has, as a rule, several small holes located around the periphery of the pipe 4 (only one hole is shown). For example, if the diameter of the pipe 4 is 25.4 mm, 8 holes with a diameter of 0.794 mm are made at the injection unit at an angle 45 downwards out of the axis of the pipe 4. The device operates as follows. A gaseous sulfating agent (a mixture of 2-10% by volume of sulfur trioxide with an inert gas, such as air) is fed through pipe 11 into pipe 3. At the same time, liquid organic reagent is fed into pipe 4 and through the injection unit 9 is sprayed into a high-speed flow of gaseous sulfating agent where it is additionally sprayed. The reaction mixture formed enters the venturi tube. 1 For more efficient spraying of liquid organic reagent, the device can be equipped (see Fig. 3) with an air supply pipe 25 covering the liquid organic reagent supply pipe 4 and having an air supply pipe 26 installed up to the liquid organic reagent injection unit 9 in the direction of air flow and the outlet end of the air supply pipe 23 protrudes beyond the injection unit 9 of the liquid organic reagent. With this structural arrangement of the device, the organic reagent is pre-sprayed with an air flow of approximately 10% of the total volume of air entering the Benturi pipe before being fed into the flow of gaseous sulfating agent. Typically, pipe 4 has an internal diameter of 3.175 mm, pipe 25 is 12.7 mm, and the diameter of the lower hole of the pipe 25 - 5.08 mm. In the Venturi Tube, the sulfonation process partially takes place. After exiting the venturi, the reaction mixture passes along body 1 and is subjected to rapid cooling (quenching) by means of oh-. of the product coming from the outlet section 10 of the pipe 5. The reaction mixture contains fine particles of liquid distributed in a gaseous medium - the carrier, and is in contact with the cooled product flowing parallel to the flow of the reaction mixture in the form of two films along the inner surface of itopnyca 1 and the outer surface of pipe 5 supply of cooled products, which causes agglomeration of small parts of liquids. The gas vortices produced in the reaction mixture reintroduce small particles of the liquid into contact with the cooled product.
    A mixture of fluid and waste. the gas leaves the housing 1 through the pipe 2 of the product outlet and passes through pipe 19 to the separator-cycle 18, in which the gas is separated from the liquid, after which the gas is removed through the pipe 21 to the atmosphere, and the liquid (product) is removed through the pipeline 17 and the pump 16 to the pipeline 15, from where a part of the product through the heat exchanger 14 enters the pipe 5 for feeding the cooled product, and a part through the pipeline 22 is supplied to. further processing, for example dehydrogenation, hydration, neutralization and hydrolysis. Part of the product from conduit 22 is recycled to the separator-cyclone 18 to flush its walls in order to prevent the accumulation of product particles.
    In the Venturi pipe, the sulfonation reaction proceeds partially and continues in the housing 1, and then in the circulating circuit - pipeline 19, separator 18, pipeline 17, pump 16, pipeline 15, heat exchanger 14, pipeline 20.
    The quality of the final product is influenced by the speed of the reaction mixture in the throat 7 of the Venturi tube, the gas velocity at the injection point of the liquid organic reagent, the temperature of the reaction mixture at the outlet of the Venturi tube, the residence time of the mixture between the injection point and the point where rapid cooling begins, and , to some extent, the size of the venturi (length and diameter of the neck).
    All these parameters are related to each other and primarily affect the degree of completion of the reaction in. Venturi tube. When the flow rate of the reaction mixture in the neck of the Venturi 233-300 m / s, the temperature reaches 93.33-148 ,. At a flow rate in the throat of 133-200 m / s, the reaction takes place in the throat only by 30-60% and the temperature is in the range of 48.89-93. The product of the flow velocity in the neck of the Venturi tube is 100,300 m / s. The optimum gas flow rate at the point of injection of the organic reagent is 17-66 m / s.
    The supply part 6 and the throat of the venturi can be cooled. However, the residence time of the reaction mixture in the venturi tube is less than 0.1 s, therefore charring of the product is not possible.
    The greater speed of the reaction mixture in the Venturi tube prevents particles from sticking on its machines. The length of the venturi also affects the degree of completeness of the reaction in it. The length of the pipe can actually be reduced by supplying the cooled product to the outlet part 8 of the Venturi tube through the slot of the assembly 24.
    The ratio of the length and diameter of the throat of the Venturi tube is kept constant when the performance changes.
    The sulfonation reaction is exothermic, which leads to an instantaneous increase in the temperature of the mixture. The temperature at the neck 7 depends on the degree of completeness of the reaction, the temperature of the loaded components and the percentage of inert diluent (air).
    In the quenching section (rapid cooling), located directly after the Venturn tube, three processes take place: cooling the reaction mixture, agglomerating small particles of liquid and reacting unreacted sulfur trioxide with an organic liquid.
    The product is cooled to a temperature above the freezing point, and this temperature is determined by the specific product and the requirements for further processing. For example, when sulfonating linear apkilbekzols, the product is cooled to a temperature below 54, and a high quality product can be obtained by cooling to 32.22-48.89C.
    When sulfonating lauripic alcohol and alpha-olefins O - 0, the product quality used is obtained at a cooling temperature of 32.22-37, and excellent quality is obtained using a cooled product with a temperature of 10-15, for alpha-olefin and about 15 ° for lauryl alcohol.
    The weight ratio of the cooled product n to the organic reagent is 10: 1. To cool the product from 93.33-176.6 to 3 7 j 78, a cooled product is required in a ratio of 60; 1,
    The diameter of most of the particles exiting the venturi is less than 1.27 mm, and some less than 0.25 mm. Such particles cannot be caught with a separator-cyclone. Therefore, they must be agglomerated, for which the reaction mixture is introduced into. contact with the film of the cooled product, small particles agglomerate, which provides for the liquid reaction product and the spent product by more than 99.8%, i.e. product loss is less than 0.2%. Typically, the length of the contact zone in the housing 1 is not less than 15.24 mm, preferably 30, 48-121.92 gv1 {the clearance gap between the housing 1 and the pipe is 5: 1, 778 Mk, the product film is 0.3048-0.5008 mm the true gas velocity in the housing 1 is 30–83 m / s and the pressure drop is O, 14–0.42 kg / cm, preferably 0.21 –0.28 kg /.
    In case I, there is also a reaction between veporagons in the Venturi tube of sulfur trioxide and liquid organic reagent. In addition, unreacted sulfur trioxide reacts with the unreacted organic reagent present; films of the cooled product (about 2-5% by weight). Due to the relatively high speed of the reaction mixture (30-83 m / s), the film thickness is 3.048-5.08 mm.
    In case 1, an excess of organic reagent is maintained with respect to sulfur trioxide in order to eliminate undesirable excess reaction between sulfur trioxide and the product in the absence of organic reagent.
    In the Venturi tube, the reaction takes place at 20-97% of the rest - mainly in case 1.
    In an embodiment, sulfur trioxide can be introduced directly into the upper quenching section, and the liquid organic reagent is introduced through conduit 25 into the cooled product before it is fed into the pipe 5, in which case the sulfonation reaction occurs entirely in the quenching section.
    The described device ensures a higher performance and quality of the product.
    FIG
    权利要求:
    Claims (5)
    [1]
    1. DEVICE FOR SULPHING AN ORGANIC REAGENT, containing a vertically mounted housing with a nozzle, a product outlet, a supply pipe of a gaseous sulfonating agent, a liquid organic reagent and a cooled product, and a heat exchanger connected by pipelines to a product discharge pipe and a pipe. Supplying a cooled product, characterized in that , in order to prevent carbonization and increase the yield of the product, it is equipped with a venturi connected to the upper part of the body with a tapering inlet, neck th and expanding outlet part, and the liquid organic reagent supply pipe is installed inside the gas supply pipe of the gaseous sulfonating agent along its axis and is equipped at the end with an injection unit located at the inlet part of the Venturi pipe, the output part of which is connected to the housing in which the pipe is concentrically mounted supply of a chilled product with an outlet assembly located at the outlet of the venturi.
    [2]
    2. The device according to π. 1, characterized in that it is provided with an air supply pipe covering the liquid organic reagent supply pipe and having an air supply pipe installed upstream of the liquid organic reagent injection unit in the air supply direction, the outlet end of the air supply pipe protruding from the liquid organic reagent injection unit .
    [3]
    3. The device according to π. 1, characterized in that it is equipped with a unit for supplying a chilled product to the outlet of the venturi.
    [4]
    4. The device according to π. 1, characterized in that it is provided with a pipe for supplying a gaseous sulfonating agent installed at an angle to the axis of the pipe for supplying a gas for sulfonating agent, in which means for smoothing the flow are mounted.
    [5]
    5. The device according to π. 1, characterized in that it is provided with an additional liquid organic 'reagent supply pipe connected to a pipe connecting the heat exchanger to the lower end of the chilled product supply pipe.
    t --- 1
    类似技术:
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    GB1111208A|1968-04-24|Process and apparatus for the continuous reaction of organic compounds with sulphur trioxide
    US3677714A|1972-07-18|Porous ring feed head
    US3839391A|1974-10-01|Method of isothermal sulfonation
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    US3232976A|1966-02-01|Sulfur trioxide sulfation and sulfonation
    US4185030A|1980-01-22|Sulfonating method
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    GB1080863A|1967-08-23|Chemically reacting gases with liquids
    US3597170A|1971-08-03|Pelletizing of carbon black directly from smoke
    同族专利:
    公开号 | 公开日
    IT1109117B|1985-12-16|
    JPS5951937B2|1984-12-17|
    FR2352767A1|1977-12-23|
    DE2723333A1|1977-12-15|
    JPS52144626A|1977-12-02|
    IN146339B|1979-05-05|
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    引用文献:
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    DE3402622C2|1984-01-26|1986-10-30|Bayer Ag, 5090 Leverkusen|Process for the preparation of diphenyl-4,4'-disulfonic acid|
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    US4812292A|1987-10-26|1989-03-14|Joslyn Valve Corporation|Chemical sterilant recovery and conversion|
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    US5211916A|1991-12-24|1993-05-18|Praxair Technology, Inc.|Stripping system|
    US5942020A|1996-01-11|1999-08-24|Tensor Machinery Limited|Apparatus for evacuating air from curing area of UV lamps for fiber-like substrates|
    CN101423482B|2008-11-27|2012-07-25|中国日用化学工业研究院|Integrated method of sulphonation and neutralization reaction|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US69065276A| true| 1976-05-27|1976-05-27|
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