CN208641854U - A kind of water-oil phase automatic separating apparatus - Google Patents

A kind of water-oil phase automatic separating apparatus Download PDF

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Publication number
CN208641854U
CN208641854U CN201821188896.0U CN201821188896U CN208641854U CN 208641854 U CN208641854 U CN 208641854U CN 201821188896 U CN201821188896 U CN 201821188896U CN 208641854 U CN208641854 U CN 208641854U
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China
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water
phase
separator
linker
port
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CN201821188896.0U
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Chinese (zh)
Inventor
侯卫波
韩龙凯
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Jin Tai Lihua Chemical Technology Co ltd
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Ji'nan Run Chemical Technology Co Ltd
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Abstract

In order to effectively be automatically separated the oily water-oil phase mixture for being mutually greater than aqueous phase densities, the utility model provides a kind of water-oil phase automatic separating apparatus, it mainly include separator, linker, the separator bottom is equipped with oily phase discharge port, top is equipped with drain, the side of separator is equipped with overflowing water port and the grease phase feed inlet under overflowing water port, the linker is connected with oily phase discharge port and pipeline maximum height is located between overflowing water port and grease phase feed inlet, balance nozzle is equipped at the top of the top of the linker and separator, equalizing main is connected between two balance nozzles, pass through the device, it can be effectively mutually automatically separated oily with water phase, accuracy is high, separation process is without human intervention.

Description

A kind of water-oil phase automatic separating apparatus
Technical field
It is the utility model relates to chemical production technical field, in particular to a kind of close greater than water phase for separating oily phase density The water-oil phase automatic separating apparatus of degree.
Background technique
At present producer after the completion of reaction kettle reacts that perhaps extractor extracts it is general using using be mounted on reaction kettle or Glass tube on extractor bottom discharge pipe is observed depending on cup, and artificial liquid separation first separates heavy phase into fluid reservoir, then Intermediate material is collected in other fluid reservoir and separated again again, finally separates light phase into special fluid reservoir i.e. It can.The apparatus structure that this method uses is simple, but precision is not high, and when discharging, field control personnel need high concentration to carry out Feed liquid observation, especially when close to two-phase interface, unless you give your whole attention to it, light phase will be clipped in heavy phase enters weight to field control personnel The fluid reservoir of phase, when purpose product is heavy phase, the precision of product will be greatly affected, for some products, even Liquid separation again is needed, the labor intensity of Field Force is huge.And even if liquid separation again, can not can also be completely secured to upper and lower two Layer material is precisely separated.
Summary of the invention
To solve the above-mentioned problems, the utility model provides a kind of water-oil phase automatic separating apparatus, for dividing automatically From oily mutually greater than the grease phase mixture in the case of aqueous phase densities, the technical solution adopted is as follows:
A kind of water-oil phase automatic separating apparatus, which is characterized in that mainly include separator, linker, the separator Bottom is equipped with oily phase discharge port, and top is equipped with drain, and the side of separator is equipped with overflowing water port and under overflowing water port Grease phase feed inlet, the linker is connected with oily phase discharge port and pipeline maximum height be located at overflowing water port and grease phase into Between material mouth, it is equipped with balance nozzle on the top of the linker and separator top, is connected between two balance nozzles flat Weigh pipeline.
Further, the overflowing water port and grease phase feed inlet are respectively positioned on the top of separator side.
Further, the overflowing water port, grease phase feed inlet, oily phase discharge port, drain, be all connected at balance nozzle There is the switch for controlling on-off.
Further, the switch is stainless steel ball valve.
Further, the linker is the flowline in " several " type.
The utility model has the beneficial effects that:
1, during liquid separation, oil is mutually flowed out from linker pipeline, and water is overflowed from overflowing water port, and is practically free of in water phase Oily phase, water phase is practically free of in oily phase, and separation is clean error free;
2, in grease phase separation, can charging continuously, while continuously liquid separation substantially increases Working efficiency, saves time cost and liquid separation process carries out in system, securely and reliably;
3, in separation process, cost of labor is saved without human intervention without human intervention;
4, the separation of grease phase mixture is carried out using the device, removes feed process, is not necessarily to other redundant power mains, more Supernumerary segment saves energy consumption.
Detailed description of the invention
Fig. 1 is water-oil phase automatic separating apparatus structural schematic diagram
Wherein, 1- separator, 2- oil phase discharge port, 3- overflowing water port, 4- grease phase feed inlet, 5- drain, 6- balance Nozzle, 7- linker, 8- equalizing main, 9- water phase liquid level line, 10- oil phase liquid bit line, L1Height of the reference line to overflowing water port Degree, L2The height that reference line is exported to bottom grease, L3Height of the reference line to balancer pipeline highest point.
Specific embodiment
With reference to the accompanying drawing 1 and specific embodiment the utility model is described in further detail.
Water-oil phase automatic separating apparatus as shown in Figure 1 mainly includes separator 1 and is connected on the outside of separator 1 Linker 7, the separator 1 staving cylindrical and bottom are inverted conical shape, and the bottom of separator is equipped with oily phase discharge port 2, Side is equipped with superposed overflowing water port 3 and the grease phase feed inlet 4 positioned at 3 following distance of overflowing water port, and top is set There is drain 5, the linker 7 is the oil pipeline in "Ji" type, 7 left side lowermost end of linker and oily 2 phase of phase discharge port Even, and the maximum height of linker 7 is located between overflowing water port 3 and grease phase feed inlet 4, and linker 7 and separator 1 are most Top is equipped with a balance nozzle 6, and equalizing main 8 is connected between two balance nozzles 6 for being connected to 1 inside of separator and connecting At logical 7 highest point of device inside pipeline.
In addition, being connected at grease phase feed inlet 4 for the feed pipe to injection grease phase mixture inside separator 1 Road is connected at overflowing water port 3 for externally drained drainage pipeline, feed pipe, drainage pipeline, with oily phase discharge port 2 Ball valve is equipped on 7 pipeline of linker of connecting place, on equalizing main 8 and 7 junction pipeline of separator 1 and linker for controlling Tubing giving sufficient strength on-off.
Specifically, in the present embodiment, the density of water is ρ1, the density of oily phase is ρ2, it is with 7 pipeline lowermost end of linker Benchmark opens an overflowing water port 3 on the top of knockout drum 1, and 3 height of overflowing water port is (L1+L2), grease phase feed inlet 4, which is located at, to be divided Middle and upper part (slightly above L from tank 12Height), pass through ρ1gL12gL22gL3Formula calculates, 7 duct height L of linker3, It sets at 7 highest point of linker after the height of pipeline, 7 lowermost end of linker is connected with oily phase discharge port 2, opens all balls Valve, oil mixing with water phase is injected into separator 1, and oil mixing with water mutually from after the entrance of grease phase feed inlet 4 of separator 1, passes through company Logical device principle and autologous density difference, AUTOMATIC ZONING, and a fixed liquid level is kept not change, oil is mutually managed from bottom linker 7 Road outflow, water phase are overflowed from overflowing water port 1, complete liquid separation work.
The above is only the preferred embodiment of the utility model, it should be pointed out that: for the common skill of the art For art personnel, without departing from the principle of this utility model, several improvement can also be made, these improvement also should be regarded as The protection scope of the utility model.

Claims (5)

1. a kind of water-oil phase automatic separating apparatus, which is characterized in that mainly include separator, linker, the separator bottom Portion is equipped with oily phase discharge port, and top is equipped with drain, and the side of separator is equipped with overflowing water port and the oil under overflowing water port Water phase feed inlet, the linker is connected with oily phase discharge port and pipeline maximum height is located at overflowing water port and grease is mutually fed Between mouthful, it is equipped with balance nozzle on the top of the linker and separator top, is connected with balance between two balance nozzles Pipeline.
2. water-oil phase automatic separating apparatus according to claim 1, which is characterized in that the overflowing water port and grease phase Feed inlet is respectively positioned on the top of separator side.
3. water-oil phase automatic separating apparatus according to claim 1, which is characterized in that the overflowing water port, grease phase Feed inlet, drain, balances the switch being respectively connected at nozzle for controlling on-off at oily phase discharge port.
4. water-oil phase automatic separating apparatus according to claim 3, which is characterized in that the switch is stainless steel ball Valve.
5. water-oil phase automatic separating apparatus according to claim 1, which is characterized in that the linker is in " several " word The flowline of type.
CN201821188896.0U 2018-07-26 2018-07-26 A kind of water-oil phase automatic separating apparatus Active CN208641854U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821188896.0U CN208641854U (en) 2018-07-26 2018-07-26 A kind of water-oil phase automatic separating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821188896.0U CN208641854U (en) 2018-07-26 2018-07-26 A kind of water-oil phase automatic separating apparatus

Publications (1)

Publication Number Publication Date
CN208641854U true CN208641854U (en) 2019-03-26

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CN201821188896.0U Active CN208641854U (en) 2018-07-26 2018-07-26 A kind of water-oil phase automatic separating apparatus

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113069793A (en) * 2021-03-19 2021-07-06 楚天华通医药设备有限公司 Liquid separation device and liquid separation system
CN114367246A (en) * 2022-01-13 2022-04-19 沈齐晖 Continuous melting and multi-phase separation system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113069793A (en) * 2021-03-19 2021-07-06 楚天华通医药设备有限公司 Liquid separation device and liquid separation system
CN114367246A (en) * 2022-01-13 2022-04-19 沈齐晖 Continuous melting and multi-phase separation system

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Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20190429

Address after: 272350 East Road north of flood prevention road, Zhang Huang Town, Yutai County, Jining, Shandong

Patentee after: Jin Tai Lihua Chemical Technology Co.,Ltd.

Address before: 250000 office building of Jinan New Material Trade Center, Tianqiao District, Jinan City, Shandong Province

Patentee before: JINAN HERUN CHEMICAL TECHNOLOGY CO.,LTD.

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: An automatic oil-water two-phase separation device

Effective date of registration: 20230927

Granted publication date: 20190326

Pledgee: Industrial and Commercial Bank of China Limited Yutai sub branch

Pledgor: Jin Tai Lihua Chemical Technology Co.,Ltd.

Registration number: Y2023980059192