CN205019874U - Big volume ordinary pressure vacuum vapour and liquid separator - Google Patents
Big volume ordinary pressure vacuum vapour and liquid separator Download PDFInfo
- Publication number
- CN205019874U CN205019874U CN201520729444.9U CN201520729444U CN205019874U CN 205019874 U CN205019874 U CN 205019874U CN 201520729444 U CN201520729444 U CN 201520729444U CN 205019874 U CN205019874 U CN 205019874U
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- cylinder
- liquid separator
- valve body
- gas
- pressure vacuum
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Abstract
The utility model discloses a big volume ordinary pressure vacuum vapour and liquid separator, including cylinder, honeycomb duct, communicating pipe, level gauge, baffle and fluid -discharge tube, the baffle sets up inside the cylinder, with inside two regions from top to bottom that divide into of cylinder, honeycomb duct one end and baffle are linked together, and the other end extends to the cylinder outside and is linked together with the lower floor region of cylinder, and are located and install first valve body on the honeycomb duct in the cylinder outside, the fluid -discharge tube is located the low head below, the regional outer peripheral face in cylinder lower floor is installed to the level gauge, both ends are connected respectively in the upper strata of cylinder is regional and the lower floor is regional about communicating pipe, and are equipped with the fourth valve body on communicating pipe. The utility model discloses big volume ordinary pressure vacuum vapour and liquid separator is equipped with the level gauge, the level gauge can according to actual fluid level control correspondingly the valve body open or close, be convenient for control the liquid level among the vapour and liquid separator, be equipped with communicating pipe on the cylinder, solved the problem that big volume vapour and liquid separator attend the pressure balance of lower floor. The effect is more outstanding.
Description
Technical field
The utility model relates to a kind of gas-liquid separator, is specifically related to a kind of large volume normal-pressure vacuum gas-liquid separator.
Background technology
Large volume Vacuum gas-liquid separator refers to the gas-liquid separator of volume more than 15 cubic metres, and gas-liquid separator, for the treatment of the gas containing lime set, realizes lime set and reclaims or gas phase purifying.Its structure is generally a pressure vessel, and inside has relevant air inlet component, drop to trap component.Gas-liquid gravity separator is the most common, and its principle utilizes the difference between liquid sedimentation speed and the gas rate of climb, separates from gas.After liquid is separated from gas, the bottom of gas-liquid separator can be temporarily stored in, when the liquid stored is too much, gas-liquid separator can be hindered normally to work, therefore, need the liquid in timing releasing gas liquid/gas separator, common Vacuum gas-liquid separator mainly through passing into gas, the liquid in malleation drainage gas-liquid separator, but for large volume vacuum pressure separator, if adopt the mode passing into gas positive pressure discharge opeing, then the time of discharge opeing is excessively slow, and efficiency is too low.Therefore, for the Design and manufacture of bulk container Vacuum gas-liquid separator also Shortcomings part in prior art, the liquid conveniently in gas-liquid separator is released, and must be further improved it.
Summary of the invention
The purpose of this utility model is the problems referred to above existed to solve prior art, provides a kind of large volume normal-pressure vacuum gas-liquid separator, is intended to make gas-liquid separator to realize automatically releasing the function of internal liquid.
Technical solution of the present utility model is: large volume normal-pressure vacuum gas-liquid separator, comprise upper cover, cylinder, low head, gas outlet pipe, breather pipe, mozzle, communicating pipe, liquid level gauge, dividing plate, gas-liquid mixture access tube and discharging tube, described upper cover and low head are installed on the two ends up and down of cylinder respectively, described dividing plate is arranged at column body, column body is divided into upper and lower two regions; Described gas outlet pipe and gas-liquid mixture access tube are all installed on the top area of cylinder, and are connected with column body, and described breather pipe is installed on the lower region of cylinder, and is connected with column body, and pressure breather pipe is provided with the 3rd valve body; Described dividing plate is provided with opening, the opening in communication of described mozzle one end and dividing plate, and the other end extends to outside cylinder and with the lower region of cylinder and is connected, and is positioned on the mozzle outside cylinder and is provided with the first valve body; Described discharging tube is positioned at below low head, and is connected with low head, and discharging tube is provided with the second valve body, and described liquid level gauge is installed on cylinder lower region outer peripheral face; Described communicating pipe, upper and lower two ends were connected to top area and the lower region of cylinder, and were all connected with the inside of cylinder, and were provided with the 4th valve body communicating pipe.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: described column body is provided with baffle plate near the position of gas-liquid mixture access tube.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: the bottom of described gas outlet pipe is provided with filter, filter is double medium filtration web frame.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: described in be positioned at outside cylinder mozzle on the first manual ball valve is installed, described discharging tube is provided with the second manual ball valve, described breather pipe is provided with the 3rd manual ball valve, is provided with the 4th manual ball valve described communicating pipe.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: described first valve body, the second valve body, the 3rd valve body are pneumatic operated valve, described 4th valve body is balance pneumatic operated valve.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: described dividing plate is recessed, described opening is arranged at the recess of dividing plate.
Further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: the top area periphery of described cylinder has manhole.
Again further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: the below of described cylinder is provided with supporting base.
Again further, above-mentioned large volume normal-pressure vacuum gas-liquid separator, wherein: described cylinder lower region is provided with upper limit level switch and bottom limit level switch.
Technique effect of the present utility model is embodied in: be provided with liquid level gauge in large volume normal-pressure vacuum gas-liquid separator, liquid level gauge can control correspondingly valve body according to actual liquid level and open or close, and is convenient to control the liquid level in gas-liquid separator; Mozzle is provided with the first manual ball valve, discharging tube is provided with the second manual ball valve, the first valve body or the second valve body malfunctioning time can promptly use, maintain equipment stablize; Filter adopts double-layer filtering net, and its filter effect is better, and the effect of gas-liquid separation is more outstanding; Cylinder is provided with communicating pipe, be provided with balance pneumatic operated valve communicating pipe, solve the pressure balanced problem of large volume gas-liquid separator levels, prevent from causing top area vacuum degradation because lower layer space is excessive, the operation relying on vacuum may be caused to produce the generation of industrial accident, lifting machine as adsorbed glass or steel plate is malfunctioning, and machining center relies on the fixing semi-finished product of negative pressure loosen and scrap.
Accompanying drawing explanation
Fig. 1 is the structural representation of large volume normal-pressure vacuum gas-liquid separator.
In figure, the implication of each Reference numeral is: 1-upper cover, 2-cylinder, 3-low head, 4-gas outlet pipe, 5-filter, 6-breather pipe, 7-mozzle, 71-the first manual ball valve, the 72-the first valve body, 8-liquid level gauge, 9-dividing plate, 10-gas-liquid mixture access tube, 11-communicating pipe, 12-upper limit level switch, 13-bottom limit level switch, 14-baffle plate, 15-manhole, 16-supporting base, 17-liquid-sighting glass, 18-discharging tube, the 181-the second manual ball valve, the 182-the second valve body.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in further detail, is easier to make technical solutions of the utility model understand and grasp.
As shown in Figure 1, the utility model relates to a kind of large volume normal-pressure vacuum gas-liquid separator, and its structure comprises: upper cover 1, cylinder 2, low head 3, gas outlet pipe 4, breather pipe 6, mozzle 7, liquid level gauge 8, dividing plate 9, gas-liquid mixture access tube 10 and discharging tube 18.Described upper cover 1 and low head 3 are installed on the two ends up and down of cylinder 2 respectively, and it is inner that dividing plate 9 is arranged at cylinder 2, and cylinder 2 inside is divided into upper and lower two regions, and top area is for holding gas, and lower region is used for receiving fluids.Gas outlet pipe 4 and gas-liquid mixture access tube 10 are all installed on the top area of cylinder 2, and be connected with cylinder 2 inside, breather pipe 6 is installed on the lower region of cylinder 2, and is connected with cylinder 2 inside, and pressure breather pipe 6 is provided with the 3rd manual ball valve and the 3rd valve body.Dividing plate 9 is provided with opening, the opening in communication of mozzle 7 one end and dividing plate 9, and the other end to extend to outside cylinder 2 and is connected with the lower region of cylinder 2, is positioned on the mozzle outside cylinder 2 and is provided with the first manual ball valve 71 and the first valve body 72.Discharging tube 18 is positioned at below low head 3, and is connected with low head 3, and discharging tube 18 is provided with the second manual ball valve 181 and the second valve body 182, and described liquid level gauge 8 is installed on cylinder 2 lower region outer peripheral face.Separately be provided with a connecting pipe 11, communicating pipe about 11, two ends were connected to top area and the lower region of cylinder 2, and be all connected with the inside of cylinder 2, be provided with the 4th valve body and the 4th manual ball valve communicating pipe 11, 4th valve body preferably balances pneumatic operated valve, its effect is to solve the pressure balanced problem of levels after separator enlarging volume, top area vacuum degradation is caused because lower layer space is excessive, the operation relying on vacuum may be caused to produce industrial accident, the generation that lifting machine as adsorbed glass or steel plate is malfunctioning, machining center relies on the fixing semi-finished product of negative pressure loosen and scrap.
As shown in Figure 1, dividing plate 9 is recessed, and opening is arranged at the recess of dividing plate.The inner position near gas-liquid mixture access tube 10 of cylinder 2 is provided with baffle plate 14, and its effect is the top area preventing liquid from entering cylinder 2.The bottom of gas outlet pipe 4 is provided with filter 5, and filter 5 has double medium filtration web frame, and its filter effect is better.The lower regions outer surface of cylinder 2 is equipped with liquid-sighting glass 17, for observing fluid level condition.Separately supporting seat is provided with, for support cylinder bottom cylinder 2.The top area periphery of cylinder 2 has manhole 15, is convenient to artificial maintenance.Described first valve body 72, second valve body 182 and the 3rd valve body are preferably pneumatic operated valve.Cylinder 2 lower region is provided with upper limit level switch 12 and bottom limit level switch 13.
Its course of work of the utility model is as follows: after gas-liquid mixture passes into from gas-liquid mixture access tube 10, liquid hydrops is in the recess of dividing plate 9, the gas of top area is pulled out and is in vacuum state, now the 4th valve body is opened, first valve body 72, second valve body 182 and the 3rd valve body are all closed, open the first valve body 72 after 8 ~ 15 seconds, liquid flow to mozzle 7 from opening, is flow to the lower region of cylinder 2 by mozzle 7; There is a magnetic float liquid level gauge 8 inside, and respectively there is a magnetic force induction switch at the two ends up and down of liquid level gauge 8, and magnetic float moves up and down with liquid level.When lower region liquid level rises, when its liquid level rises to liquid level gauge 8 upper end, upper end liquid-level switch triggers upper limit level switch 12, then the first valve body closedown 72 and the 4th valve body are closed, and the second valve body 182 and the 3rd valve body are opened, breather pipe 6 is opened, lower region is communicated with air, in atmospheric pressure state, and, connect suction pump in discharging tube 18 lower end, under the effect of suction pump and atmospheric pressure, lower floor's liquid is discharged rapidly; When liquid level drops to the lower end of liquid level gauge 8, the liquid-level switch of lower end triggers bottom limit level switch 13, then the first valve body 72 is opened, and the 4th valve body generation opened, and the second valve body 182 and the 3rd valve body are closed, and liquid continues to flow into lower region, circulates with this.When the first valve body 72, second valve body 182, when there is the situation that damage cannot use or need to finely tune each air valve in the 3rd valve body or the 4th valve body, can use the first manual ball valve, the second manual ball valve, the 3rd manual ball valve or the 4th manual ball valve, mode manually regulates each manual ball valve to complete corresponding action.
By describing above and can finding out, large volume normal-pressure vacuum gas-liquid separator is provided with liquid level gauge, and liquid level gauge can control correspondingly valve body according to actual liquid level and open or close, and is convenient to control the liquid level in gas-liquid separator; Mozzle is provided with the first manual ball valve, discharging tube is provided with the second manual ball valve, can promptly use when valve body is malfunctioning, the equipment that maintains is stablized; Filter adopts double-layer filtering net, and its filter effect is better, and the effect of gas-liquid separation is more outstanding; Cylinder is provided with communicating pipe, be provided with balance pneumatic operated valve communicating pipe, solve the pressure balanced problem of large volume gas-liquid separator levels, top area vacuum degradation is caused because lower layer space is excessive, the operation relying on vacuum may be caused to produce the generation of industrial accident, lifting machine as adsorbed glass or steel plate is malfunctioning, and machining center relies on the fixing semi-finished product of negative pressure loosen and scrap.
Certainly, be more than representative instance of the present utility model, in addition, the utility model can also have other multiple detailed description of the invention, and all employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop within the claimed scope of the utility model.
Claims (9)
1. large volume normal-pressure vacuum gas-liquid separator, it is characterized in that: comprise upper cover, cylinder, low head, gas outlet pipe, breather pipe, mozzle, communicating pipe, liquid level gauge, dividing plate, gas-liquid mixture access tube and discharging tube, described upper cover and low head are installed on the two ends up and down of cylinder respectively, described dividing plate is arranged at column body, column body is divided into upper and lower two regions; Described gas outlet pipe and gas-liquid mixture access tube are all installed on the top area of cylinder, and are connected with column body, and described breather pipe is installed on the lower region of cylinder, and is connected with column body, and pressure breather pipe is provided with the 3rd valve body; Described dividing plate is provided with opening, the opening in communication of described mozzle one end and dividing plate, and the other end extends to outside cylinder and with the lower region of cylinder and is connected, and is positioned on the mozzle outside cylinder and is provided with the first valve body; Described discharging tube is positioned at below low head, and is connected with low head, and discharging tube is provided with the second valve body, and described liquid level gauge is installed on cylinder lower region outer peripheral face; Described communicating pipe, upper and lower two ends were connected to top area and the lower region of cylinder, and were all connected with the inside of cylinder, and were provided with the 4th valve body communicating pipe.
2. large volume normal-pressure vacuum gas-liquid separator according to claim 1, is characterized in that: described column body is provided with baffle plate near the position of gas-liquid mixture access tube.
3. large volume normal-pressure vacuum gas-liquid separator according to claim 1, it is characterized in that: the bottom of described gas outlet pipe is provided with filter, filter is double medium filtration web frame.
4. large volume normal-pressure vacuum gas-liquid separator according to claim 1, it is characterized in that: described in be positioned at outside cylinder mozzle on the first manual ball valve is installed, described discharging tube is provided with the second manual ball valve, described breather pipe is provided with the 3rd manual ball valve, is provided with the 4th manual ball valve described communicating pipe.
5. large volume normal-pressure vacuum gas-liquid separator according to claim 1, is characterized in that: described first valve body, the second valve body, the 3rd valve body are pneumatic operated valve, and described 4th valve body is balance pneumatic operated valve.
6. large volume normal-pressure vacuum gas-liquid separator according to claim 1, it is characterized in that: described dividing plate is recessed, described opening is arranged at the recess of dividing plate.
7. large volume normal-pressure vacuum gas-liquid separator according to claim 1, is characterized in that: the top area periphery of described cylinder has manhole.
8. large volume normal-pressure vacuum gas-liquid separator according to claim 1, is characterized in that: the below of described cylinder is provided with supporting base.
9. large volume normal-pressure vacuum gas-liquid separator according to claim 1, is characterized in that: described cylinder lower region is provided with upper limit level switch and bottom limit level switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520729444.9U CN205019874U (en) | 2015-09-18 | 2015-09-18 | Big volume ordinary pressure vacuum vapour and liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520729444.9U CN205019874U (en) | 2015-09-18 | 2015-09-18 | Big volume ordinary pressure vacuum vapour and liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205019874U true CN205019874U (en) | 2016-02-10 |
Family
ID=55252442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520729444.9U Expired - Fee Related CN205019874U (en) | 2015-09-18 | 2015-09-18 | Big volume ordinary pressure vacuum vapour and liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205019874U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107529446A (en) * | 2017-09-13 | 2018-01-02 | 江苏新凯晟机械设备有限公司 | Can be from the Vacuum gas-liquid separator of discharge opeing |
| CN107583390A (en) * | 2017-10-16 | 2018-01-16 | 五洲丰农业科技有限公司 | Vacuum gas-liquid separator and separation method |
| CN107617237A (en) * | 2017-10-18 | 2018-01-23 | 新乡市恒星科技有限责任公司 | A kind of lubricating grease continuous degassing device |
| CN114345036A (en) * | 2022-02-18 | 2022-04-15 | 崔汉博 | Semiconductor waste gas treatment equipment with water-vapor separation device and treatment method |
-
2015
- 2015-09-18 CN CN201520729444.9U patent/CN205019874U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107529446A (en) * | 2017-09-13 | 2018-01-02 | 江苏新凯晟机械设备有限公司 | Can be from the Vacuum gas-liquid separator of discharge opeing |
| CN107583390A (en) * | 2017-10-16 | 2018-01-16 | 五洲丰农业科技有限公司 | Vacuum gas-liquid separator and separation method |
| CN107617237A (en) * | 2017-10-18 | 2018-01-23 | 新乡市恒星科技有限责任公司 | A kind of lubricating grease continuous degassing device |
| CN114345036A (en) * | 2022-02-18 | 2022-04-15 | 崔汉博 | Semiconductor waste gas treatment equipment with water-vapor separation device and treatment method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160210 Termination date: 20200918 |