CN101972571A - Spiral-flow type spray catcher - Google Patents

Spiral-flow type spray catcher Download PDF

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Publication number
CN101972571A
CN101972571A CN 201010550657 CN201010550657A CN101972571A CN 101972571 A CN101972571 A CN 101972571A CN 201010550657 CN201010550657 CN 201010550657 CN 201010550657 A CN201010550657 A CN 201010550657A CN 101972571 A CN101972571 A CN 101972571A
Authority
CN
China
Prior art keywords
tank body
pipe
spiral
flow type
mist eliminator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN 201010550657
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Chinese (zh)
Inventor
王守波
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
VERITAS-MSI
Original Assignee
VERITAS-MSI
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by VERITAS-MSI filed Critical VERITAS-MSI
Priority to CN 201010550657 priority Critical patent/CN101972571A/en
Publication of CN101972571A publication Critical patent/CN101972571A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a spiral-flow type spray catcher, comprising a tank body (1); the top of the tank body (1) is provided with an air outlet pipe (12), the side is provided with an input pipe (11), the bottom is provided with a drain pipe (13); wherein the input pipe (11) is tangent with the side of the tank body (1), the air outlet pipe (12) is stretched into the central interior of the tank body (1) from the top of the tank body (1), and an opening at the bottom end (12a) of the air outlet pipe (12) is taken as the inlet of the air outlet pipe (12). Compared with the prior art, the spray catcher provided by the invention has the advantages that gas and liquid circulation is smooth in the tank body, processing speed of tank body can be greatly improved, working efficiency of spray catcher can be improved, meanwhile centrifugation force is utilized, drop catching capability is strong, and gas liquid separation effect is ideal.

Description

The spiral-flow type mist eliminator
Technical field
The invention belongs to the technical field that gas-liquid separation is handled, be meant a kind of spiral-flow type mist eliminator that can carry out gas-liquid separation especially.
Background technology
Mist eliminator uses comparatively general in oil, natural gas extraction and separating treatment.Existing mist eliminator generally comprises tank body and is filled in the interior intensive coagulated material of tank body, wherein, the tank body top has the input port, the bottom has delivery outlet, and the intensive silk screen that interweaves of the general employing of the coagulated material in the tank body is such as crisscross woven wire, solid type filter screen or the like.During actual the use, gas-liquid mixed fog enters in the tank body from the input port, by coagulated material with the droplets agglomerate in the fog after, liquid is from the delivery outlet output of bottom.As all having used similar mist eliminator in the Chinese utility model patent " the integrated high precision measurement device of memory-type temperature and pressure " that the patent No. is the Chinese utility model patent " the compound separator of natural gas " of ZL200620078754.X, Chinese utility model patent " drilling fluid two-stage degasification equipment " that the patent No. is ZL200620007889.7, the patent No. is ZL200820090257.0.But existing mist eliminator because whole tank body has been expired in the coagulated material filling, makes the interior top-down circulation of liquid of tank body significantly be obstructed, and causes flow velocity slow excessively, and the operating efficiency of mist eliminator is restricted.The more important thing is, outlet of an inlet only is set in the mist eliminator, the outlet of isolating with the liquid output channel of specializing in the gas discharge is not set, and when real work, the gas-liquid mixed fog that enters from the input port is the input of band certain pressure, gas can't rise to the input port and can only discharge from delivery outlet, like this, can mix with the liquid of discharging again again from delivery outlet, though the drop in the fog forms liquid by coagulated material, but last gas still can mix with liquid, does not realize gas-liquid separation, gas-liquid separation is handled helping not quite.Therefore, existing mist eliminator needs further improvement.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of spiral-flow type mist eliminator that can realize good gas-liquid separation effect simultaneously at the present situation of prior art, gas in its tank body, liquid communication are unimpeded, can significantly increase the processing speed of tank body, improve the operating efficiency of mist eliminator.
The present invention solves the problems of the technologies described above the technical scheme that is adopted: this spiral-flow type mist eliminator, comprise tank body, it is characterized in that: this tank body top is provided with that escape pipe, sidewall are provided with input pipe, the bottom is provided with drain pipe, wherein, the sidewall of this input pipe and tank body is tangent, and described escape pipe extend into the central interior of tank body from the top of tank body, the bottom end opening of this escape pipe and as the inlet of escape pipe.
The gas that is entrained with drop tangentially is input in the tank body of mist eliminator, and at tank body generation eddy flow, utilize action of centrifugal force, relatively heavier drop is thrown to inner tank wall and flow into the drain pipe of tank base along inwall, lighter gas then is pooled to tank body central authorities relatively, the bottom opening of the escape pipe of central authorities enters into escape pipe in extending into tank body, exports from the top of escape pipe at last.
Preferably, can also be provided with a liquid level gauge communicating pipe on the sidewall of described tank body, and connect liquid level gauge, with stable control mist eliminator.
Because the mist eliminator volume is less relatively, the bottom of described mist eliminator tank body can be provided with a support, in order to the high whole mist eliminator of frame.
Compared with prior art, the invention has the advantages that: gas in the tank body of mist eliminator, liquid communication are unimpeded, can significantly increase the processing speed of tank body, improve the operating efficiency of mist eliminator, simultaneously, the present invention utilizes action of centrifugal force, and it is strong to catch the drop ability, make bring about the desired sensation, the liquid separating effect is very desirable.
Description of drawings
Fig. 1 is the structural representation of the embodiment of the invention.
The specific embodiment
Embodiment describes in further detail the present invention below in conjunction with accompanying drawing.
As shown in Figure 1, this spiral-flow type mist eliminator comprises tank body 1, and this tank body 1 top is provided with that escape pipe 12, sidewall are provided with input pipe 11, the bottom is provided with drain pipe 13;
Simultaneously, this input pipe 11 is tangent with the sidewall of tank body 1, and described escape pipe 12 extend into the central interior of tank body 1 from the top of tank body 1, the bottom 12a opening of this escape pipe 12 and as the inlet of escape pipe 12, the bottom of tank body 1 is provided with a support 14, and the height of this support 14 is looked actual needs and adjusted.

Claims (3)

1. spiral-flow type mist eliminator, comprise tank body (1), it is characterized in that: this tank body (1) top is provided with that escape pipe (12), sidewall are provided with input pipe (11), the bottom is provided with drain pipe (13), wherein, this input pipe (11) is tangent with the sidewall of tank body (1), and described escape pipe (12) extend into the central interior of tank body (1) from the top of tank body (1), bottom (12a) opening of this escape pipe (12) and as the inlet of escape pipe (12).
2. spiral-flow type mist eliminator according to claim 1 is characterized in that: also be provided with a liquid level gauge communicating pipe (15) on the sidewall of described tank body (1).
3. spiral-flow type mist eliminator according to claim 1 is characterized in that: the bottom of described tank body (1) is provided with a support (14).
CN 201010550657 2010-11-11 2010-11-11 Spiral-flow type spray catcher Pending CN101972571A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010550657 CN101972571A (en) 2010-11-11 2010-11-11 Spiral-flow type spray catcher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201010550657 CN101972571A (en) 2010-11-11 2010-11-11 Spiral-flow type spray catcher

Publications (1)

Publication Number Publication Date
CN101972571A true CN101972571A (en) 2011-02-16

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201010550657 Pending CN101972571A (en) 2010-11-11 2010-11-11 Spiral-flow type spray catcher

Country Status (1)

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CN (1) CN101972571A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110302597A (en) * 2018-03-20 2019-10-08 汉科系统科技股份有限公司 The gas-liquid separation device of tail gas
CN112521993A (en) * 2020-11-13 2021-03-19 重庆科技学院 Natural gas foam separation device, control method and application

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201055811Y (en) * 2007-04-19 2008-05-07 宁波威瑞泰默赛多相流仪器设备有限公司 Rotational flow type gas-liquid separater
CN101664624A (en) * 2009-09-21 2010-03-10 宁波威瑞泰默赛多相流仪器设备有限公司 Mist catcher
CN101664720A (en) * 2009-09-21 2010-03-10 宁波威瑞泰默赛多相流仪器设备有限公司 Spiral-flow type gas, oil and water separator
CN201959657U (en) * 2010-11-11 2011-09-07 宁波威瑞泰默赛多相流仪器设备有限公司 Spiral-flow type spray catcher

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201055811Y (en) * 2007-04-19 2008-05-07 宁波威瑞泰默赛多相流仪器设备有限公司 Rotational flow type gas-liquid separater
CN101664624A (en) * 2009-09-21 2010-03-10 宁波威瑞泰默赛多相流仪器设备有限公司 Mist catcher
CN101664720A (en) * 2009-09-21 2010-03-10 宁波威瑞泰默赛多相流仪器设备有限公司 Spiral-flow type gas, oil and water separator
CN201959657U (en) * 2010-11-11 2011-09-07 宁波威瑞泰默赛多相流仪器设备有限公司 Spiral-flow type spray catcher

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110302597A (en) * 2018-03-20 2019-10-08 汉科系统科技股份有限公司 The gas-liquid separation device of tail gas
CN112521993A (en) * 2020-11-13 2021-03-19 重庆科技学院 Natural gas foam separation device, control method and application

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Application publication date: 20110216