Paraffin online emulsification system

By setting up premix tanks and circulation pipelines in the paraffin online emulsification system, the problems of poor emulsification and difficulty in recycling and recycling of existing online emulsification equipment are solved, and efficient emulsification and resource reuse are achieved.

CN222468859UActive Publication Date: 2025-02-14ZHANGZHOU JIELONG AUTOMATION TECH
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Patent Information

Application Number
CN202420106304.5
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-01-16
Publication Date
2025-02-14
Estimated Expiration
2034-01-16

AI Technical Summary

Technical Problem

When the existing online emulsification equipment has poor emulsification effect and the emulsified paraffin dispersion cannot meet the use requirements, it is difficult to recycle and reuse.

Method used

A paraffin online emulsification system is designed, including a liquid supply device, a raw material tank, an emulsification device, a buffer tank and a premix tank. Premix is ​​performed by setting a premix tank before the emulsification device, and a circulation tube is provided at the output end of the emulsification device. to achieve recycling and reuse of paraffin dispersions that do not meet the requirements of use.

Benefits of technology

The emulsification effect is improved, the quality of the emulsified paraffin dispersion is ensured, and the effective recycling and reuse of paraffin dispersion that cannot meet the usage requirements is achieved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model provides a paraffin online emulsification system which comprises a liquid supply device, a raw material tank, an emulsification device, a buffer tank and a premixing tank, the output end of the emulsification device is connected with the buffer tank through a first pipeline, and the output end of the buffer tank is connected with a paraffin dispersion liquid output pipeline; the output end of the liquid supply device is connected with the input end of the premixing tank through a second pipeline, the output end of the raw material tank is connected with the input end of the premixing tank through a third pipeline, and the output end of the premixing tank is connected with the input end of the emulsifying device through a fourth pipeline; the output end of the emulsifying device is provided with a first circulating pipeline communicated with the input end of the premixing tank, and the first circulating pipeline is provided with a first control valve. The paraffin dispersion liquid emulsifying device has the advantages that the premixing tank is arranged in front of the emulsifying device, so that the emulsifying effect can be improved, the quality of emulsified paraffin dispersion liquid is ensured, and meanwhile, the paraffin dispersion liquid which cannot meet the use requirement can be well recycled due to the arrangement of the first circulating pipeline.
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Description

[Technical field]

[0001] The utility model relates to the technical field of paraffin emulsification, in particular to an online paraffin emulsification system. [Background technology]

[0002] Paraffin dispersion can be used as a waterproofing agent and is widely used in waterproofing of artificial boards. In the past, after the paraffin dispersion was produced, it was usually cooled first and then the packaged paraffin dispersion was transported to the customer's production site for use. This method is not only costly, but also the paraffin dispersion is prone to precipitation and solidification.

[0003] Of course, there are also devices in the prior art that can be installed at the production site and used for online emulsification of paraffin, such as the Chinese utility model patent with application number 201920339492.5, which discloses an online emulsification and dispersion device that can automatically select the formula raw materials. The online emulsification device can be set up at the customer's production site, which is conducive to controlling product quality, and can select the formula of the emulsion (i.e., paraffin dispersion). However, the above existing online emulsification equipment has the following defects in the actual production process: the melted liquid paraffin and emulsifier or dispersant aqueous solution are directly transported to the emulsification device for emulsification, and the emulsification effect is not good. When the emulsified paraffin dispersion cannot meet the use requirements, it is difficult to recycle and reuse the paraffin dispersion. In view of the above-mentioned problems, the inventor of this case conducted an in-depth study on the problem, and thus this case came into being. [Contents of the utility model]

[0004] The technical problem to be solved by the utility model is to provide an online paraffin emulsification system to solve the problem that the existing online emulsification equipment has poor emulsification effect and it is difficult to recycle and reuse the paraffin dispersion when the emulsified paraffin dispersion cannot meet the use requirements.

[0005] The utility model is implemented as follows: a paraffin online emulsification system, comprising a liquid supply device, a raw material tank, an emulsification device, a buffer tank and a premixing tank, wherein the output end of the emulsification device is connected to the buffer tank through a first pipeline, and the output end of the buffer tank is connected to a paraffin dispersion output pipeline;

[0006] The output end of the liquid supply device is connected to the input end of the premixing tank through a second pipeline, the output end of the raw material tank is connected to the input end of the premixing tank through a third pipeline, the output end of the premixing tank is connected to the input end of the emulsification device through a fourth pipeline, and the output end of the emulsification device has a first circulation pipeline connected to the input end of the premixing tank, and the first circulation pipeline is equipped with a first control valve.

[0007] Further, the liquid supply device includes a first preparation tank, a second preparation tank, a first metering tank, a second metering tank and a hot water storage tank, the volume of the first preparation tank is greater than the volume of the first metering tank, and the volume of the second preparation tank is greater than the volume of the second metering tank;

[0008] The output end of the first preparation tank is connected to the input end of the first metering tank through the fifth pipeline, the output end of the second preparation tank is connected to the input end of the second metering tank through the sixth pipeline, the output end of the first metering tank, the output end of the second metering tank and the output end of the hot water storage tank are all connected to the input end of the premixing tank through the second pipeline; the output end of the hot water storage tank is also connected to the output end of the first metering tank, the output end of the second metering tank and the output end of the cache tank through the seventh pipeline, and the seventh pipeline is equipped with a second control valve.

[0009] Furthermore, a second circulation pipeline is provided between the output end and the input end of the cache tank, and a third control valve is provided on the second circulation pipeline.

[0010] Furthermore, a first stirring mechanism is provided at a middle position of the inner bottom of the premixing tank, a second stirring mechanism is provided at a middle position of the inner top of the premixing tank, and a third stirring mechanism is provided around the second stirring mechanism at the inner top of the premixing tank; a fourth stirring mechanism is provided at a middle position of the inner top of the second preparation tank, and a fifth stirring mechanism is provided at a middle position of the inner top of the cache tank; the first stirring mechanism and the third stirring mechanism are high-speed stirring mechanisms, and the second stirring mechanism, the fourth stirring mechanism and the fifth stirring mechanism are low-speed stirring mechanisms.

[0011] Furthermore, there are two raw material tanks, one of which is used as a main tank and the other is used as a backup tank.

[0012] Furthermore, there are at least two cache tanks.

[0013] Furthermore, it also includes a heat transfer oil supply device; the raw material tank, premixing tank, buffer tank and hot water storage tank are all wound with heat transfer oil coils, each of the heat transfer oil coils is connected to the heat transfer oil supply device through a heat transfer oil circulation pipeline, and the heat transfer oil circulation pipeline is equipped with a fourth control valve.

[0014] Furthermore, the first pipeline, the third pipeline, the fourth pipeline, the first circulation pipeline, the paraffin dispersion output pipeline and the second circulation pipeline are all provided with insulation pipes on the outside, and the insulation pipes are connected to the heat transfer oil supply device.

[0015] Furthermore, it also includes a cooling water supply device; a cooling coil is also wound around the premixing tank, and the cooling coil is connected to the cooling water supply device through a cooling water circulation pipeline.

[0016] Furthermore, the raw material tank, buffer tank, first preparation tank, second preparation tank, first metering tank, second metering tank and hot water storage tank are all equipped with weighing sensors, liquid level sensors and temperature sensors; the second pipeline, the third pipeline and the paraffin dispersion output pipeline are all provided with flow meters.

[0017] By adopting the technical solution of the utility model, at least the following beneficial effects are achieved:

[0018] 1. A premixing tank is set before the emulsifying device. When in use, hot water, dispersant, additives and liquid paraffin will be premixed in the premixing tank and then transported to the emulsifying device for emulsification, which can improve the emulsification effect and ensure the quality of the emulsified paraffin dispersion.

[0019] 2. The output end of the emulsifying device has a first circulation pipeline connected to the input end of the premixing tank. The first circulation pipeline is equipped with a first control valve, so that when the emulsified paraffin dispersion cannot meet the use requirements, the first control valve can be opened to return the paraffin dispersion output by the emulsifying device to the premixing tank through the first circulation pipeline, so that the paraffin dispersion that cannot meet the use requirements can enter the emulsifying device for re-emulsification. Therefore, the paraffin dispersion that cannot meet the use requirements can be well recycled and reused, which is very convenient to use.

[0020] 3. The liquid supply device is designed to have a first preparation tank, a second preparation tank, a first metering tank and a second metering tank, and the volume of the first preparation tank is larger than that of the first metering tank, and the volume of the second preparation tank is larger than that of the second metering tank. In specific use, the first preparation tank can be used to prepare more additives in advance and the second preparation tank can be used to prepare more dispersants, so that the required additives can be provided to the first metering tank in real time and the required dispersants can be provided to the second metering tank in real time.

[0021] 4. By setting a second circulation pipeline between the output end and the input end of the buffer tank, and setting a third control valve on the second circulation pipeline, when the buffer tank does not need to provide paraffin dispersion to the production line in actual use, the third control valve can be opened to put the paraffin dispersion in a circulating flow state, thereby avoiding the coagulation and precipitation of the paraffin dispersion due to long-term stagnation.

[0022] 5. A first stirring mechanism is arranged in the middle of the inner bottom of the premixing tank, a second stirring mechanism is arranged in the middle of the inner top of the premixing tank, and a third stirring mechanism is arranged around the second stirring mechanism, and both the first stirring mechanism and the third stirring mechanism are high-speed stirring mechanisms, so that in specific work, the first stirring mechanism, the second stirring mechanism and the third stirring mechanism can be used to cooperate to fully stir the hot water, dispersant, additives and liquid paraffin transported to the premixing tank, so that the hot water, dispersant, additives and liquid paraffin can be better mixed together, thereby improving the subsequent emulsification effect; at the same time, a fourth stirring mechanism is arranged on the inner top of the second preparation tank, which can facilitate the preparation of the dispersant; a fifth stirring mechanism is arranged on the inner top of the buffer tank, and the fifth stirring mechanism can be used to stir and disturb the paraffin dispersion stored in the buffer tank, so that the paraffin dispersion in the buffer tank is not prone to coagulation and precipitation.

[0023] 5. The online emulsification system is designed with two raw material tanks, one main and one backup. When the raw material tank as the main tank is unable to provide the required liquid paraffin to the pre-mixing tank in time due to an abnormality, it can be switched to the raw material tank as the backup tank in time, thereby ensuring that the required paraffin dispersion can be prepared online in real time.

[0024] 6. Insulated pipes are installed outside the first pipeline, the third pipeline, the fourth pipeline, the first circulation pipeline, the paraffin dispersion output pipeline and the second circulation pipeline, and the insulating pipes are connected to the heat transfer oil supply device, so that when in use, the heat transfer oil provided by the heat transfer oil supply device can be circulated into the insulating pipes, thereby insulating the first pipeline, the third pipeline, the fourth pipeline, the first circulation pipeline, the paraffin dispersion output pipeline and the second circulation pipeline, ensuring that the liquid paraffin will not solidify during the transportation process.

[0025] 7. A cooling coil is further provided on the premixing tank, and the cooling coil is connected to a cooling water supply device through a cooling water circulation pipeline. When the temperature in the premixing tank is too high, the cooling water supply device can provide cooling water to the cooling coil through the cooling water circulation pipeline to cool it down, thereby adjusting the temperature in the premixing tank.

Brief Description of the Drawings

[0026] The present invention will be further described below in conjunction with the embodiments with reference to the accompanying drawings.

[0027] Figure 1 This is a schematic diagram of the overall structure of an online paraffin emulsification system of the utility model;

[0028] Figure 2 It is a structural schematic diagram of the liquid supply device in the utility model;

[0029] Figure 3It is a structural schematic diagram of the premixing tank in the utility model;

[0030] Figure 4 It is a structural schematic diagram of the raw material tank in the utility model;

[0031] Figure 5 It is a structural schematic diagram of the cache tank in the utility model.

[0032] Description of reference numerals:

[0033] Liquid supply device 1, second pipeline 11, first preparation tank 12, second preparation tank 13, first metering tank 14, second metering tank 15, hot water storage tank 16, fifth pipeline 17, sixth pipeline 18, seventh pipeline 19, second control valve 191;

[0034] Raw material tank 2, third pipeline 21;

[0035] Emulsifying device 3, first pipeline 31, first circulation pipeline 32, first control valve 33;

[0036] Buffer tank 4, paraffin dispersion output pipeline 41, second circulation pipeline 42, third control valve 43;

[0037] Premixing tank 5, fourth pipeline 51;

[0038] A first stirring mechanism 61, a second stirring mechanism 62, a third stirring mechanism 63, a fourth stirring mechanism 64, and a fifth stirring mechanism 65;

[0039] A heat transfer oil supply device 71, a heat transfer oil coil 72, a heat transfer oil circulation pipeline 73, a fourth control valve 74, and a heat preservation pipeline 75;

[0040] Cooling water supply device 81, cooling coil 82, cooling water circulation pipeline 83;

[0041] Weighing sensor 91 , liquid level sensor 92 , temperature sensor 93 , flow meter 94 , second sewage valve 941 , sampling valve 942 , first sewage valve 95 , fifth control valve 96 , pressure transmitter 97 , duplex filter 98 . [Specific implementation method]

[0042] In order to better understand the technical solution of the present invention, the technical solution of the present invention will be described in detail below in conjunction with the accompanying drawings and specific implementation methods.

[0043] It should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", etc., indicate positions or positional relationships based on the positions or positional relationships shown in the drawings, and are only for the convenience of describing these embodiments and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation. In addition, the terms "first", "second", etc., etc. are only used for descriptive purposes, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, features defined as "first", "second", etc. may explicitly or implicitly include one or more of the features.

[0044] See also Figures 1 to 5 As shown, a preferred embodiment of the utility model is a paraffin online emulsification system, the online emulsification system comprises a liquid supply device 1, a raw material tank 2, an emulsification device 3, a buffer tank 4 and a premixing tank 5, wherein the liquid supply device 1 is used to provide hot water, dispersant and additives, the raw material tank 2 is used to provide paraffin, the premixing tank 5 is used to premix the hot water, dispersant, additives and liquid paraffin, the emulsification device 3 is used to emulsify the premixed hot water, dispersant, additives and liquid paraffin, and the buffer tank 4 is used to store the emulsified paraffin dispersion;

[0045] The output end of the emulsifying device 3 is connected to the buffer tank 4 through the first pipeline 31, so that the paraffin dispersion emulsified by the emulsifying device 3 is transported to the buffer tank 4 through the first pipeline 31 for storage; the output end of the buffer tank 4 is connected to the paraffin dispersion output pipeline 41, so that the paraffin dispersion is transported to the production line through the paraffin dispersion output pipeline 41 for use; the output end of the liquid supply device 1 is connected to the input end of the premixing tank 5 through the second pipeline 11, so that the hot water, dispersant and additives provided by the liquid supply device 1 are transported to the premixing tank 5 through the second pipeline 11; the output end of the raw material tank 2 is connected to the input end of the premixing tank 5 through the third pipeline 21, so that the liquid paraffin provided by the raw material tank 2 is transported to the premixing tank 5 through the third pipeline 21 is transported to the premixing tank 5; the output end of the premixing tank 5 is connected to the input end of the emulsifying device 3 through a fourth pipeline 51, so as to realize the transportation of the hot water, dispersant, additive and liquid paraffin premixed in the premixing tank 5 to the emulsifying device 3 for emulsification; and the output end of the emulsifying device 3 has a first circulation pipeline 32 connected to the input end of the premixing tank 5, and the first circulation pipeline 32 is equipped with a first control valve 33, which is in a closed state under normal working conditions. One or more first control valves 33 can be set, and when there are multiple first control valves 33, some of the first control valves 33 can be designed as manual valves, and the other part of the first control valves 33 can be designed as electric valves.

[0046] By adopting the above technical solution of the utility model, at least the following beneficial effects are achieved:

[0047] 1. A premixing tank 5 is provided before the emulsifying device 3. When in use, hot water, dispersant, additives and liquid paraffin are premixed in the premixing tank 5 and then transported to the emulsifying device 3 for emulsification, which can improve the emulsification effect and thus ensure the quality of the emulsified paraffin dispersion.

[0048] 2. The output end of the emulsifying device 3 has a first circulation pipeline 32 connected to the input end of the premixing tank 5. The first circulation pipeline 32 is equipped with a first control valve 33, so that when the emulsified paraffin dispersion cannot meet the use requirements, the first control valve 33 can be opened to return the paraffin dispersion output by the emulsifying device 3 to the premixing tank 5 through the first circulation pipeline 32, so that the paraffin dispersion that cannot meet the use requirements can enter the emulsifying device 3 for re-emulsification. Therefore, the paraffin dispersion that cannot meet the use requirements can be well recycled and reused, which is very convenient to use.

[0049] In a preferred embodiment of the utility model, the liquid supply device 1 includes a first preparation tank 12, a second preparation tank 13, a first metering tank 14, a second metering tank 15 and a hot water storage tank 16, the volume of the first preparation tank 12 is greater than the volume of the first metering tank 14, and the volume of the second preparation tank 13 is greater than the volume of the second metering tank 15; wherein the first preparation tank 12 is used to prepare additives, the second preparation tank 13 is used to prepare dispersants, the first metering tank 14 is used to meter additives, the second metering tank 15 is used to meter dispersants, and the hot water storage tank 16 is used to provide the required hot water;

[0050] The output end of the first preparation tank 12 is connected to the input end of the first metering tank 14 through the fifth pipeline 17, so that the additive prepared by the first preparation tank 12 is transported to the first metering tank 14 through the fifth pipeline 17; the output end of the second preparation tank 13 is connected to the input end of the second metering tank 15 through the sixth pipeline 18, so that the dispersant prepared by the second preparation tank 13 is transported to the second metering tank 15 through the sixth pipeline 18; the output end of the first metering tank 14, the output end of the second metering tank 15 and the output end of the hot water storage tank 16 are all connected to the input end of the premixing tank 5 through the second pipeline 11, so that the additive, dispersant and hot water are transported to the second metering tank 15 through the second pipeline 11. 1 is transported to the premixing tank 5; the output end of the hot water storage tank 16 is also connected to the output ends of the first metering tank 14, the output end of the second metering tank 15 and the output end of the buffer tank 4 through the seventh pipeline 19, and the seventh pipeline 19 is equipped with a second control valve 191, so as to use the seventh pipeline 19 to provide the required hot water to the output ends of the first metering tank 14, the output end of the second metering tank 15 and the output end of the buffer tank 4; specifically, one or more second control valves 191 can be provided, and when there are multiple second control valves 191, some of the second control valves 191 can be designed as manual valves, and the other part of the second control valves 191 can be designed as electric valves.

[0051] As a specific implementation of the utility model, the volume of the first preparation tank 12, the second preparation tank 13 and the hot water storage tank 16 is designed to be 1000L, the volume of the first metering tank 14 and the second metering tank 15 is 500L, the volume of the raw material tank 2 is 500L, and the volume of the premixing tank 5 and the buffer tank 4 is 1000L.

[0052] The utility model designs a liquid supply device 1 with a first preparation tank 12, a second preparation tank 13, a first metering tank 14 and a second metering tank 15, and the volume of the first preparation tank 12 is greater than the volume of the first metering tank 14, and the volume of the second preparation tank 13 is greater than the volume of the second metering tank 15, so that in specific use, the first preparation tank 12 can be used to prepare more additives in advance and the second preparation tank 13 can be used to prepare more dispersants, so that the required additives can be conveniently provided to the first metering tank 14 in real time and the required dispersants can be conveniently provided to the second metering tank 15 in real time.

[0053] In a preferred embodiment of the utility model, a second circulation pipeline 42 is arranged between the output end and the input end of the buffer tank 4, and a third control valve 43 is arranged on the second circulation pipeline 42. When the buffer tank 4 needs to provide paraffin dispersion to the production line, the third control valve 43 is in a closed state, and when the buffer tank 4 does not need to provide paraffin dispersion to the production line, the third control valve 43 is in an open state; the third control valve 43 can be set to one or more, and when there are multiple third control valves 43, some of the third control valves 43 can be designed as manual valves, and the other part of the third control valves 43 can be designed as electric valves.

[0054] The utility model adopts a method of setting a second circulation pipeline 42 between the output end and the input end of the buffer tank 4, and setting a third control valve 43 on the second circulation pipeline 42, so that in actual use, when the buffer tank 4 does not need to provide paraffin dispersion to the production line, the third control valve 43 can be opened to put the paraffin dispersion in a circulating flow state, thereby preventing the paraffin dispersion from solidifying and precipitating due to long-term stillness.

[0055] In a preferred embodiment of the utility model, a first stirring mechanism 61 is provided at a middle position of the inner bottom of the premixing tank 5, a second stirring mechanism 62 is provided at a middle position of the inner top of the premixing tank 5, and a third stirring mechanism 63 is provided around the second stirring mechanism 62 at the inner top of the premixing tank 5; a fourth stirring mechanism 64 is provided at a middle position of the inner top of the second preparation tank 13, and a fifth stirring mechanism 65 is provided at a middle position of the inner top of the cache tank 4; the first stirring mechanism 61 and the third stirring mechanism 63 are high-speed stirring mechanisms, and the second stirring mechanism 62, the fourth stirring mechanism 64 and the fifth stirring mechanism 65 are low-speed stirring mechanisms.

[0056] The utility model sets a first stirring mechanism 61 in the middle of the inner bottom of the premixing tank 5, sets a second stirring mechanism 62 in the middle of the inner top of the premixing tank 5, and sets a third stirring mechanism 63 around the second stirring mechanism 62, and the first stirring mechanism 61 and the third stirring mechanism 63 are both high-speed stirring mechanisms, so that in specific operation, the first stirring mechanism 61, the second stirring mechanism 62 and the third stirring mechanism 63 can be used to cooperate to fully stir the hot water, dispersant, additives and liquid paraffin transported to the premixing tank 5, so that the hot water, dispersant, additives and liquid paraffin can be better mixed together, thereby improving the subsequent emulsification effect; at the same time, the inner top of the second preparation tank 13 is provided with a fourth stirring mechanism 64, which can facilitate the preparation of the dispersant; the inner top of the buffer tank 4 is provided with a fifth stirring mechanism 65, which can be used to stir and disturb the paraffin dispersion stored in the buffer tank 4, so that the paraffin dispersion in the buffer tank 4 is not prone to coagulation and precipitation.

[0057] In a preferred embodiment of the utility model, there are two raw material tanks 2, one of which is used as a main tank and the other is used as a backup tank. By designing the online emulsification system to have two raw material tanks 2, one main and one backup, when the raw material tank 2 as the main tank fails to provide the required liquid paraffin to the premixing tank 5 in time due to an abnormality, it can be switched to the raw material tank 2 as the backup tank in time, thereby ensuring that the required paraffin dispersion can be prepared online in real time.

[0058] In a preferred embodiment of the present utility model, there are at least two buffer tanks 4, so that it is convenient to provide the required paraffin dispersion to multiple production lines at the same time, and the prepared paraffin dispersion can be better stored.

[0059] In a preferred embodiment of the utility model, the online emulsification system also includes a heat transfer oil supply device 71; the raw material tank 2, the premixing tank 5, the cache tank 4 and the hot water storage tank 16 are all wound with a heat transfer oil coil 72, each of the heat transfer oil coils 72 is connected to the heat transfer oil supply device 71 through a heat transfer oil circulation pipeline 73, and the heat transfer oil circulation pipeline 73 is provided with a fourth control valve 74. More specifically, the heat transfer oil circulation pipeline 73 is provided with a fourth control valve 74 at the input end position and the output end position corresponding to the raw material tank 2, the premixing tank 5, the cache tank 4 and the hot water storage tank 16, so as to facilitate the control of the delivery of the heat transfer oil; when working, the heat transfer oil output by the heat transfer oil supply device 71 can be delivered to the raw material tank 2, the premixing tank 5, the cache tank 4 and the hot water storage tank 16 through the heat transfer oil circulation pipeline 73 for use, so as to utilize the heat transfer oil to realize the heating function.

[0060] In a preferred embodiment of the present utility model, the first pipeline 31 , the third pipeline 21 , the fourth pipeline 51 , the first circulation pipeline 32 , the paraffin dispersion output pipeline 41 and the second circulation pipeline 42 are all provided with an insulation pipe 75 outside, and the insulation pipe 75 is connected to the heat transfer oil supply device 71 .

[0061] Since liquid paraffin is easy to solidify, an insulating pipe 75 is installed on the outside of the first pipeline 31, the third pipeline 21, the fourth pipeline 51, the first circulation pipeline 32, the paraffin dispersion output pipeline 41 and the second circulation pipeline 42, and the insulating pipe 75 is connected to the heat transfer oil supply device 71. When in use, the heat transfer oil provided by the heat transfer oil supply device 71 can be circulated into the insulating pipe 75, thereby insulating the first pipeline 31, the third pipeline 21, the fourth pipeline 51, the first circulation pipeline 32, the paraffin dispersion output pipeline 41 and the second circulation pipeline 42, thereby ensuring that the liquid paraffin will not solidify during the transportation process.

[0062] In a preferred embodiment of the utility model, the online emulsification system further includes a cooling water supply device 81; a cooling coil 82 is also wound around the premixing tank 5, and the cooling coil 82 is connected to the cooling water supply device 81 through a cooling water circulation pipeline 83. Since the temperature in the premixing tank 5 may be high during operation, the premixing tank 5 is further provided with a cooling coil 82, and the cooling coil 82 is connected to the cooling water supply device 81 through a cooling water circulation pipeline 83, so that when the temperature in the premixing tank 5 is high, the cooling water supply device 81 can provide cooling water to the cooling coil 82 through the cooling water circulation pipeline 83 to cool it down, thereby adjusting the temperature in the premixing tank 5.

[0063] In a preferred embodiment of the present utility model, the raw material tank 2, the buffer tank 4, the first preparation tank 12, the second preparation tank 13, the first metering tank 14, the second metering tank 15 and the hot water storage tank 16 are all equipped with a weighing sensor 91, a liquid level sensor 92 and a temperature sensor 93, wherein the weighing sensor 91 is used to realize the weighing function, so as to facilitate the mixing of hot water, dispersant, additives and liquid paraffin according to the required proportion; the liquid level sensor 92 is used to realize liquid level detection. When the raw material tank 2, the cache tank 4, the first preparation tank 12, the second preparation tank 13, the first metering tank 14, the second metering tank 15 and the hot water storage tank 16 are used, liquid level sensors 92 may be provided at the upper and lower parts to detect low and high liquid levels; the temperature sensor 93 is used to detect the temperature of the medium (such as hot water, dispersant, additive, liquid paraffin) in the raw material tank 2, the cache tank 4, the first preparation tank 12, the second preparation tank 13, the first metering tank 14, the second metering tank 15 and the hot water storage tank 16.

[0064] The second pipeline 11, the third pipeline 21 and the paraffin dispersion output pipeline 41 are all provided with flow meters 94, wherein the second pipeline 11 is provided with flow meters 94 at the output ends of the first metering tank 14, the second metering tank 15 and the hot water storage tank 16, so as to detect the medium flow in the pipe by using the flow meters 94. In the specific implementation of the utility model, both ends of each flow meter 94 are equipped with a second drain valve 941 and a sampling valve 942, so as to facilitate draining and sampling operations.

[0065] The bottoms of the raw material tank 2, the buffer tank 4, the first preparation tank 12, the second preparation tank 13, the first metering tank 14, the second metering tank 15 and the hot water storage tank 16 are all provided with a first drain valve 95 for draining. The first pipeline 31, the second pipeline 11, the third pipeline 21, the fourth pipeline 51, the fifth pipeline 17, the sixth pipeline 18 and the paraffin dispersion output pipeline 41 are all provided with a fifth control valve 96, and a plurality of the fifth control valves 96 may be provided, and some of the fifth control valves 96 may be designed to be manual valves, and the other part of the fifth control valves 96 may be electric valves. The first pipeline 31, the second pipeline 11, the third pipeline 21, the fourth pipeline 51, the fifth pipeline 17, the sixth pipeline 18, the paraffin dispersion output pipeline 41 and the heat transfer oil circulation pipeline 73 can be equipped with a pressure transmitter 97 to detect the pressure in the first pipeline 31, the second pipeline 11, the third pipeline 21, the fourth pipeline 51, the fifth pipeline 17, the sixth pipeline 18, the paraffin dispersion output pipeline 41 and the heat transfer oil circulation pipeline 73. The fifth pipeline 17 and the sixth pipeline 18 are also provided with a double filter 98 to play a filtering role. The third pipeline 21, the fourth pipeline 51, the paraffin dispersion output pipeline 41 and the heat transfer oil circulation pipeline 73 are also equipped with a temperature sensor 93 to detect the medium temperature in the second pipeline 11, the third pipeline 21, the fourth pipeline 51, the paraffin dispersion output pipeline 41 and the heat transfer oil circulation pipeline 73.

[0066] Although the specific implementation methods of the present invention are described above, those skilled in the art should understand that the specific embodiments described are only illustrative and are not intended to limit the scope of the present invention. Equivalent modifications and changes made by those skilled in the art in accordance with the spirit of the present invention should be included in the scope of protection of the claims of the present invention.

Claims

1. A paraffin online emulsification system, comprising a liquid supply device, a raw material tank, an emulsification device and a buffer tank, wherein the output end of the emulsification device is connected to the buffer tank through a first pipeline, and the output end of the buffer tank is connected to a paraffin dispersion output pipeline; characterized in that: Also included are pre-mix tanks; The output end of the liquid supply device is connected to the input end of the premixing tank through a second pipeline, the output end of the raw material tank is connected to the input end of the premixing tank through a third pipeline, the output end of the premixing tank is connected to the input end of the emulsification device through a fourth pipeline, and the output end of the emulsification device has a first circulation pipeline connected to the input end of the premixing tank, and the first circulation pipeline is equipped with a first control valve.

2. A paraffin online emulsification system as claimed in claim 1, characterized in that: The liquid supply device comprises a first preparation tank, a second preparation tank, a first metering tank, a second metering tank and a hot water storage tank; the volume of the first preparation tank is greater than the volume of the first metering tank, and the volume of the second preparation tank is greater than the volume of the second metering tank; The output end of the first preparation tank is connected to the input end of the first metering tank through the fifth pipeline, the output end of the second preparation tank is connected to the input end of the second metering tank through the sixth pipeline, the output end of the first metering tank, the output end of the second metering tank and the output end of the hot water storage tank are all connected to the input end of the premixing tank through the second pipeline; the output end of the hot water storage tank is also connected to the output end of the first metering tank, the output end of the second metering tank and the output end of the cache tank through the seventh pipeline, and the seventh pipeline is equipped with a second control valve.

3. A paraffin online emulsification system as claimed in claim 2, characterized in that: A second circulation pipeline is provided between the output end and the input end of the cache tank, and a third control valve is arranged on the second circulation pipeline.

4. A paraffin online emulsification system as claimed in claim 2, characterized in that: A first stirring mechanism is arranged at a middle position of the inner bottom of the premixing tank, a second stirring mechanism is arranged at a middle position of the inner top of the premixing tank, and a third stirring mechanism is arranged around the second stirring mechanism at the inner top of the premixing tank; a fourth stirring mechanism is arranged at a middle position of the inner top of the second preparation tank, and a fifth stirring mechanism is arranged at a middle position of the inner top of the buffer tank; the first stirring mechanism and the third stirring mechanism are high-speed stirring mechanisms, and the second stirring mechanism, the fourth stirring mechanism and the fifth stirring mechanism are low-speed stirring mechanisms.

5. A paraffin online emulsification system as claimed in claim 1, characterized in that: There are two raw material tanks, one of which is used as a main tank and the other is used as a backup tank.

6. A paraffin online emulsification system as claimed in claim 1, characterized in that: There are at least two cache tanks.

7. A paraffin online emulsification system as claimed in claim 3, characterized in that: It also includes a heat transfer oil supply device; the raw material tank, premixing tank, buffer tank and hot water storage tank are all wound with heat transfer oil coils, each of the heat transfer oil coils is connected to the heat transfer oil supply device through a heat transfer oil circulation pipeline, and the heat transfer oil circulation pipeline is equipped with a fourth control valve.

8. A paraffin online emulsification system as claimed in claim 7, characterized in that: The first pipeline, the third pipeline, the fourth pipeline, the first circulation pipeline, the paraffin dispersion output pipeline and the second circulation pipeline are all provided with insulation pipelines outside, and the insulation pipelines are connected to the heat transfer oil supply device.

9. A paraffin online emulsification system as claimed in claim 7, characterized in that: It also includes a cooling water supply device; a cooling coil is wound around the premixing tank, and the cooling coil is connected to the cooling water supply device through a cooling water circulation pipeline.

10. A paraffin online emulsification system as claimed in claim 2, characterized in that: The raw material tank, buffer tank, first preparation tank, second preparation tank, first metering tank, second metering tank and hot water storage tank are all equipped with weighing sensors, liquid level sensors and temperature sensors; the second pipeline, the third pipeline and the paraffin dispersion output pipeline are all provided with flow meters.

Citation Information

Patent Citations

  • Online emulsifying and dispersing equipment capable of automatically selecting formula raw materials

    CN210613401U