CN212870804U - Oil gas sprays condensing tank - Google Patents
Oil gas sprays condensing tank Download PDFInfo
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- CN212870804U CN212870804U CN202021478922.0U CN202021478922U CN212870804U CN 212870804 U CN212870804 U CN 212870804U CN 202021478922 U CN202021478922 U CN 202021478922U CN 212870804 U CN212870804 U CN 212870804U
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Abstract
An oil gas spraying condensing tank relates to the field of oil gas condensing equipment. The condenser pipe spiral sets up in the jar internally, and the condenser pipe inlet outlet is fixed in jar side wall, condenser pipe inlet outlet part is the circular duct, and the condenser pipe main part is flat elliptical tube, and the suction pump is connected with the fluid-discharge tube, and circulating pipe one end is connected the other end with the suction pump and upwards is fixed in jar side wall and extends into jar internally, the circulating pipe still contains horizontal shower, vertical shower, and the internal bottom pond of level gauge valve intercommunication jar, atmospheric pressure detector set up in jar body top, and the blast pipe sets up in jar body top, and discharge valve is connected with the blast pipe, and the inlet tube sets up in jar side wall, and the fourth control valve is connected. The cooling area in unit time is increased by adopting an elliptical condensation pipe body, the condensation pipe is sprayed and covered transversely and longitudinally in an all-around manner, and the cooling efficiency is improved to the maximum extent.
Description
Technical Field
The utility model relates to an oil gas sprays condensing tank relates to oil gas condensation equipment field.
Background
In the modern industry, certain high temperature oil gas can exist in many production and processing links, some high temperature oil gas does not contain harmful substances, some high temperature oil gas contains harmful substances, the oil gas containing harmless substances can be generally recycled, if the oil gas is directly discharged, certain waste can be caused, if an oil tank truck unloads oil at a gas station, the high temperature oil gas generated in an oil tank can be discharged along with the oil unloading, the long-time accumulation can cause great waste, if the oil gas containing harmful substances is directly discharged, the harm can be caused to the surrounding environment and the health of operating personnel, and some dangerous oil gas mixtures can even explode, thereby bringing harm to the safety of social and property.
In order to solve the problem of direct emission of oil gas, the common practice in the prior art is to treat oil gas by adopting a condensation method, the oil gas flows in a condensation pipe after entering the condensation equipment, one type of condensation equipment adopts a soaking mode to cool the condensation pipe, the condensation pipe is completely immersed in cold water or cooling liquid to rapidly cool, high-temperature steam is rapidly cooled to form condensed water after being in indirect contact with the cold water through the condensation pipe, the oil floats on the water surface due to the fact that the weight of the oil is lighter than that of the water, the oil-water separation effect is achieved, the oil-water separation device is used for separating and recycling the oil and the water, on the one hand, harmful substances are separated and recycled, but more cold water or cooling liquid is needed to be used by the condensation equipment; another kind adopts the tank deck to set up the shower head, and the mode to the cooling of condenser pipe water spray is with high-temperature steam condensation, trades water after cooling water temperature is too high, and the mode that sprays compares and soaks the cooling and has saved a large amount of water resources, nevertheless only sprays cooling water first half at the condenser pipe usually when spraying, and the comdenstion water formation speed is slow, and the cooling effect is not good enough, needs to increase the length of condenser pipe usually and improves cooling efficiency.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to prior art's defect and not enough, provide an oil gas sprays condensate tank, increase condenser pipe area of contact through adopting flat condenser pipe, the cooling effect increases substantially in same unit interval, multistage shower head acts on the condenser pipe simultaneously, and the all-round covers that sprays to the condenser pipe, and cooling rate is fast, sets up the atmospheric pressure detection device simultaneously, and the atmospheric pressure in the real-time detection condensate tank prevents that the interior atmospheric pressure of jar is too high to appear unexpected, has guaranteed production operation safety.
In order to achieve the above purpose, the utility model adopts the following technical scheme: the water-saving type solar water heater comprises a tank body 1, a condensation pipe 2, a water suction pump 3, a circulating pipe 4, a liquid level meter 5, an air pressure detector 6, a spherical spray head 7, a first control valve 8, a second control valve 9, a liquid discharge pipe 10, a water discharge pipe 11, a third control valve 12, an exhaust pipe 13, an exhaust valve 14, a water inlet pipe 15, a fourth control valve 16 and a water tank 17, wherein the condensation pipe 2 is spirally arranged in the tank body 1, the water inlet and outlet of the condensation pipe 2 are fixed on the side wall of the tank body 1, the water inlet and outlet of the condensation pipe 2 are circular pipes, the main part of the condensation pipe 2 is a flat elliptical pipe, the liquid discharge pipe 10 is arranged at the bottom of the tank body 1, the water suction pump 3 is connected with the liquid discharge pipe 10, one end of the circulating pipe 4 is connected with the water suction pump 3, the other end of the circulating pipe is upwards fixed on the side wall of the tank, On the vertical shower 4-2, the pond 17 sets up in 1 bottoms of the jar body, level gauge 5 sets up in 1 lateral wall of the jar body, level gauge 5 valve intercommunication 1 interior bottom pond 17 of the jar body, atmospheric pressure detector 6 sets up in 1 tops of the jar body, first control valve 8 is installed in 2 water inlets of condenser pipe, second control valve 9 is installed in 2 water outlets of condenser pipe, drain pipe 11 is connected with fluid-discharge tube 10, third control valve 12 is installed in drain pipe 11, blast pipe 13 sets up in 1 tops of the jar body, discharge valve 14 is connected with blast pipe 13, inlet tube 15 sets up in 1 lateral wall of the jar body, fourth control valve 16 is connected with inlet tube 15.
Further, the liquid level meter 5 is a magnetic turning plate liquid level meter.
Further, the condensation pipe 2 is in a spiral arrangement structure.
Furthermore, the connecting part of the condensation pipe 2 and the water inlet and outlet is in a bell mouth shape.
Furthermore, seven spherical spray headers 7 are arranged on the transverse spray pipe 4-1.
Furthermore, the longitudinal spray pipe 4-2 is provided with four spherical spray headers 7.
Furthermore, a temperature detector 18 is further arranged on the side wall of the tank body 1, and the temperature detector 18 is composed of a thermocouple and a display screen.
The utility model discloses a theory of operation: opening a fourth control valve 16 to inject cooling water into a water inlet pipe 15 into a water tank 17, starting a water suction pump 3, pumping the cooling water out of the water tank 17 through a liquid discharge pipe 10 and entering a circulating pipe 4, dividing the cooling water into a transverse spray pipe 4-1 and a longitudinal spray pipe 4-2 after entering a tank body 1, spraying the cooling water out of a spherical spray head 7, opening a first control valve 8 to inject oil gas into the water inlet pipe of a condensation pipe 2, cooling the oil gas by the cooling water sprayed out of the transverse spray pipe 4-1 provided with seven spherical spray heads 7 when the oil gas passes through an elliptical pipe main body, wherein the cooling area is increased to the maximum extent by the elliptical pipe main body, so that the water vapor can be rapidly condensed to form condensed water and separate oil, when oil-gas mixed liquid circulates in the condensation pipe 2, the upper surface pipe is cooled by the spherical spray head 7 arranged on the transverse spray pipe 4-1, and the longitudinal spray pipe 4-2 can spray and cool the longitudinal pipe body, the magnetic turning plate type liquid level meter 5 can detect the cooling water level of a water tank 17 most intuitively and effectively, the temperature detector 18 is used for detecting the temperature of the cooling water, the third control valve 12 is opened to discharge and recover the cooling water after the temperature of the cooling water is too high, the fourth control valve 16 is opened and the third control valve 12 is closed to inject new cooling water after the water level is discharged according to the display of the liquid level meter 5, the oil-gas mixed liquid is repeatedly recycled, the oil-gas mixed liquid is completely cooled to form oil-water mixed liquid when flowing from the top to the bottom, the second control valve 9 is opened to discharge the oil-water mixed liquid to an oil-water separation device to recover oil and water, and in the condensation process, the temperature of the cooling water rises and can be gasified to generate steam after being heated for a long time, so that the pressure in the tank body 1 rises, the air pressure detector 6 detects the air pressure in the tank body 1 in real time, and when the air pressure is detected to be too high, the exhaust valve 14 is opened to discharge the air from the exhaust pipe 13 to the air recovery device.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without inventive exercise.
Fig. 1 is a schematic structural diagram of the present invention;
fig. 2 is a view of the condensation duct 2 of fig. 1 in the direction of a.
Description of reference numerals: the device comprises a tank body 1, a condensation pipe 2, a water suction pump 3, a circulating pipe 4, a liquid level meter 5, an air pressure detector 6, a spherical spray head 7, a first control valve 8, a second control valve 9, a liquid discharge pipe 10, a water discharge pipe 11, a third control valve 12, an exhaust pipe 13, an exhaust valve 14, a water inlet pipe 15, a fourth control valve 16, a water tank 17, a temperature detector 18, a transverse spray pipe 4-1 and a longitudinal spray pipe 4-2.
Detailed Description
Referring to fig. 1 to 2, the technical solution adopted by the present embodiment is: the water-saving and environment-friendly water-saving tank comprises a tank body 1, a condensation pipe 2, a water suction pump 3, a circulating pipe 4, a liquid level meter 5, an air pressure detector 6, a spherical spray head 7, a first control valve 8, a second control valve 9, a liquid discharge pipe 10, a water discharge pipe 11, a third control valve 12, an exhaust pipe 13, an exhaust valve 14, a water inlet pipe 15, a fourth control valve 16 and a water tank 17, wherein the condensation pipe 2 is spirally arranged in the tank body 1, the water inlet and outlet of the condensation pipe 2 are fixed on the side wall of the tank body 1, the water inlet and outlet of the condensation pipe 2 are circular pipes, the main part of the condensation pipe 2 is a flat elliptical pipe, the liquid discharge pipe 10 is arranged at the bottom of the tank body 1, the water suction pump 3 is connected with the liquid discharge pipe 10, one end of the circulating pipe 4 is connected with the water suction pump 3, the other end of the circulating pipe 4 is upwards fixed on the side wall of, On the vertical shower 4-2, the pond 17 sets up in 1 bottoms of the jar body, level gauge 5 sets up in 1 lateral wall of the jar body, level gauge 5 valve intercommunication 1 interior bottom pond 17 of the jar body, atmospheric pressure detector 6 sets up in 1 tops of the jar body, first control valve 8 is installed in 2 water inlets of condenser pipe, second control valve 9 is installed in 2 water outlets of condenser pipe, drain pipe 11 is connected with fluid-discharge tube 10, third control valve 12 is installed in drain pipe 11, blast pipe 13 sets up in 1 tops of the jar body, discharge valve 14 is connected with blast pipe 13, inlet tube 15 sets up in 1 lateral wall of the jar body, fourth control valve 16 is connected with inlet tube 15. Opening a fourth control valve 16 to inject cooling water into a water inlet pipe 15 into a water tank 17, starting a water suction pump 3, pumping the cooling water out of the water tank 17 through a liquid discharge pipe 10 and entering a circulating pipe 4, dividing the cooling water into a transverse spray pipe 4-1 and a longitudinal spray pipe 4-2 after entering a tank body 1, spraying the cooling water out of a spherical spray head 7, opening a first control valve 8 to inject oil gas into the water inlet pipe of a condensation pipe 2, cooling the oil gas by the cooling water sprayed out of the transverse spray pipe 4-1 provided with seven spherical spray heads 7 when the oil gas passes through an elliptical pipe main body, wherein the cooling area is increased to the maximum extent by the elliptical pipe main body, so that the water vapor can be rapidly condensed to form condensed water and separate oil, when oil-gas mixed liquid circulates in the condensation pipe 2, the upper surface pipe is cooled by the spherical spray head 7 arranged on the transverse spray pipe 4-1, and the longitudinal spray pipe 4-2 can spray and cool the longitudinal pipe body, can also spray and cool the bottom surface of the pipe body, and the omnidirectional spray cooling can achieve the purposes of being most efficient and saving cooling water
Further, the liquid level meter 5 is a magnetic turning plate liquid level meter. The magnetic turning plate liquid level meter displays more accurately.
Further, the condensation pipe 2 is in a spiral arrangement structure. The flat elliptical tube body with the spiral arrangement structure has larger contact area and better cooling effect.
Furthermore, the connecting part of the condensation pipe 2 and the water inlet and outlet is in a bell mouth shape. The pressure intensity is increased when oil-gas mixed liquid enters the flat-mouth pipe body from the circular-mouth water inlet pipe, the flow speed is increased, and the cooling efficiency is improved.
Furthermore, seven spherical spray headers 7 are arranged on the transverse spray pipe 4-1. Seven spherical showerheads 7 can cover a larger area of the tube.
Furthermore, the longitudinal spray pipe 4-2 is provided with four spherical spray headers 7. The longitudinally-arranged spray headers can cover the side wall of the pipe body and the bottom of the pipe body, so that the cooling efficiency is improved.
Furthermore, a temperature detector 18 is further arranged on the side wall of the tank body 1, and the temperature detector 18 is composed of a thermocouple and a display screen. The thermocouple is simple to use and has more accurate detection effect.
The utility model discloses a theory of operation: opening a fourth control valve 16 to inject cooling water into a water inlet pipe 15 into a water tank 17, starting a water suction pump 3, pumping the cooling water out of the water tank 17 through a liquid discharge pipe 10 and entering a circulating pipe 4, dividing the cooling water into a transverse spray pipe 4-1 and a longitudinal spray pipe 4-2 after entering a tank body 1, spraying the cooling water out of a spherical spray head 7, opening a first control valve 8 to inject oil gas into the water inlet pipe of a condensation pipe 2, cooling the oil gas by the cooling water sprayed out of the transverse spray pipe 4-1 provided with seven spherical spray heads 7 when the oil gas passes through an elliptical pipe main body, wherein the cooling area is increased to the maximum extent by the elliptical pipe main body, so that the water vapor can be rapidly condensed to form condensed water and separate oil, when oil-gas mixed liquid circulates in the condensation pipe 2, the upper surface pipe is cooled by the spherical spray head 7 arranged on the transverse spray pipe 4-1, and the longitudinal spray pipe 4-2 can spray and cool the longitudinal pipe body, the magnetic turning plate type liquid level meter 5 can detect the cooling water level of a water tank 17 most intuitively and effectively, the temperature detector 18 is used for detecting the temperature of the cooling water, the third control valve 12 is opened to discharge and recover the cooling water after the temperature of the cooling water is too high, the fourth control valve 16 is opened and the third control valve 12 is closed to inject new cooling water after the water level is discharged according to the display of the liquid level meter 5, the oil-gas mixed liquid is repeatedly recycled, the oil-gas mixed liquid is completely cooled to form oil-water mixed liquid when flowing from the top to the bottom, the second control valve 9 is opened to discharge the oil-water mixed liquid to an oil-water separation device to recover oil and water, and in the condensation process, the temperature of the cooling water rises and can be gasified to generate steam after being heated for a long time, so that the pressure in the tank body 1 rises, the air pressure detector 6 detects the air pressure in the tank body 1 in real time, and when the air pressure is detected to be too high, the exhaust valve 14 is opened to discharge the air from the exhaust pipe 13 to the air recovery device.
After the technical scheme is adopted, the utility model discloses beneficial effect does: the cooling area in unit time is increased by adopting an elliptical condensation pipe body, the condensation pipe is sprayed and covered transversely and longitudinally in an all-around manner, and the cooling efficiency is improved to the maximum extent.
The above description is only for the purpose of illustrating the technical solutions of the present invention and not for the purpose of limiting the same, and other modifications or equivalent replacements made by those of ordinary skill in the art to the technical solutions of the present invention should be covered within the scope of the claims of the present invention as long as they do not depart from the spirit and scope of the technical solutions of the present invention.
Claims (7)
1. The oil gas spraying condensing tank is characterized in that: the device comprises a tank body (1), a condensation pipe (2), a water suction pump (3), a circulating pipe (4), a liquid level meter (5), an air pressure detector (6), a spherical spray header (7), a first control valve (8), a second control valve (9), a liquid discharge pipe (10), a water discharge pipe (11), a third control valve (12), an exhaust pipe (13), an exhaust valve (14), a water inlet pipe (15), a fourth control valve (16) and a water pool (17), wherein the condensation pipe (2) is spirally arranged in the tank body (1), a water inlet and a water outlet of the condensation pipe (2) are fixed on the side wall of the tank body (1), the water inlet and the water outlet of the condensation pipe (2) are round pipes, the main body part of the condensation pipe (2) is a flat elliptic pipe, the liquid discharge pipe (10) is arranged at the bottom of the tank body (1), the water suction pump (3) is connected with the liquid discharge pipe (10), one end of the circulating pipe (4) is connected with the water suction, the circulating pipe (4) also comprises a transverse spraying pipe (4-1) and a longitudinal spraying pipe (4-2), a spherical spraying head (7) is arranged on the transverse spraying pipe (4-1) and the longitudinal spraying pipe (4-2), a water pool (17) is arranged at the bottom of the tank body (1), a liquid level meter (5) is arranged on the side wall of the tank body (1), a valve of the liquid level meter (5) is communicated with the water pool (17) at the bottom in the tank body (1), an air pressure detector (6) is arranged at the top of the tank body (1), a first control valve (8) is arranged at a water inlet of the condensing pipe (2), a second control valve (9) is arranged at a water outlet of the condensing pipe (2), a drain pipe (11) is connected with a liquid discharge pipe (10), a third control valve (12) is arranged at the drain pipe (11), an exhaust pipe (13) is arranged at the top of the tank body (1), an exhaust valve (14) is connected with the, the fourth control valve (16) is connected with the water inlet pipe (15).
2. The oil and gas spray condensing tank of claim 1, wherein: the liquid level meter (5) is a magnetic turning plate liquid level meter.
3. The oil and gas spray condensing tank of claim 1, wherein: the condensation pipe (2) is in a spiral arrangement structure.
4. The oil and gas spray condensing tank of claim 1, wherein: the connecting part of the condensation pipe (2) and the water inlet and outlet is in a bell mouth shape.
5. The oil and gas spray condensing tank of claim 1, wherein: seven spherical spray headers (7) are arranged on the transverse spray pipe (4-1).
6. The oil and gas spray condensing tank of claim 1, wherein: the longitudinal spray pipe (4-2) is provided with four spherical spray headers (7).
7. The oil and gas spray condensing tank of claim 1, wherein: the side wall of the tank body (1) is also provided with a temperature detector (18), and the temperature detector (18) consists of an electric thermocouple and a display screen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021478922.0U CN212870804U (en) | 2020-07-24 | 2020-07-24 | Oil gas sprays condensing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021478922.0U CN212870804U (en) | 2020-07-24 | 2020-07-24 | Oil gas sprays condensing tank |
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| Publication Number | Publication Date |
|---|---|
| CN212870804U true CN212870804U (en) | 2021-04-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202021478922.0U Active CN212870804U (en) | 2020-07-24 | 2020-07-24 | Oil gas sprays condensing tank |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113758060A (en) * | 2021-08-23 | 2021-12-07 | 陈胜举 | Evaporative condenser for refrigerating system |
| CN116878297A (en) * | 2023-07-11 | 2023-10-13 | 湖北清江水电开发有限责任公司 | Forced water-cooling oil collecting respirator started automatically in grading manner and operation method thereof |
-
2020
- 2020-07-24 CN CN202021478922.0U patent/CN212870804U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113758060A (en) * | 2021-08-23 | 2021-12-07 | 陈胜举 | Evaporative condenser for refrigerating system |
| CN113758060B (en) * | 2021-08-23 | 2022-12-23 | 深圳英创能源环境技术有限公司 | Evaporative condenser for refrigerating system |
| CN116878297A (en) * | 2023-07-11 | 2023-10-13 | 湖北清江水电开发有限责任公司 | Forced water-cooling oil collecting respirator started automatically in grading manner and operation method thereof |
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