CN104258642B - A kind of natural gas filter - Google Patents

A kind of natural gas filter Download PDF

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Publication number
CN104258642B
CN104258642B CN201410537002.4A CN201410537002A CN104258642B CN 104258642 B CN104258642 B CN 104258642B CN 201410537002 A CN201410537002 A CN 201410537002A CN 104258642 B CN104258642 B CN 104258642B
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filter
filter mechanism
natural gas
cylindrical shell
shunt conduit
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CN104258642A (en
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秦祖奎
朱亮
苏黎辉
康仑
胡然
崔志权
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SICHUAN DEYANG SHENGFA PETROLEUM TOOL CO Ltd
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SICHUAN DEYANG SHENGFA PETROLEUM TOOL CO Ltd
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Abstract

The invention discloses a kind of natural gas filter, comprise first and second identical filter mechanism of structure and shunt conduit, bus dump; The two ends correspondence of shunt conduit is connected to the front portion of first and second axial arranged filter mechanism, shunt conduit is provided with air inlet, and the shunt conduit be provided with between the first stop valve and the second filter mechanism of the shunt conduit between air inlet and the first filter mechanism is provided with the second stop valve; The two ends correspondence of bus dump is connected to the rear portion of first and second filter mechanism, bus dump is provided with gas outlet, and the bus dump be provided with between the 3rd stop valve and the second filter mechanism of the bus dump between gas outlet and the first filter mechanism is provided with the 4th stop valve.Effectively and define Redundancy Design reliably, two filter mechanisms can not only filter cleaning natural gas Primordial Qi simultaneously, and can also be formed each other " spare tyre ", thus guarantee that natural gas transmission pipeline normally runs, reliable and practical in the present invention.

Description

A kind of natural gas filter
Technical field
The invention discloses a kind of cleaning equipment of natural gas Primordial Qi, specifically a kind of natural gas filter.
Background technology
Due to technical measures such as supercharging exploitations, exploit in the natural gas Primordial Qi obtained and have a large amount of solid, liquid impurity, these impurity determine Primordial Qi directly can not flow to terminal use, and the natural gas namely flowing to terminal use must through removal of impurities filtration treatment.
At present, common natural gas filter is monomer operation, namely on the feed-line of natural gas Primordial Qi, only arranges a filter mechanism in a series arrangement.This filter type not only filtration yield is limited; and because of the cleaned at regular intervals of filter mechanism and unscheduled maintenance etc., need often to carry out " shutdown " to feed-line, this has had a strong impact on the purification conveying capacity of natural gas Primordial Qi; add the operation cost of natural gas transport enterprise, very impracticable.
In addition, natural gas filtering mechanism is formed primarily of cylindrical shell and the filter core be assemblied in cylindrical shell, and common filter core is screen cloth, and it is reliable that this filter core is used for filtering solid contaminants.But, exploit the natural gas Primordial Qi obtained to be carried up by boost fluid, namely liquid gas is mixing one, aforementioned filter core cannot make the gas-liquid separation in Primordial Qi effectively, need to purchase separately and the essence filter equipment-separator being series at filter mechanism rear portion carries out gas-liquid separation in Primordial Qi (certainly, also need to remove fine-particle solid impurity), the cleaning mode of this smart filter equipment that Primordial Qi gas-liquid separation is placed one's entire reliance upon, the loss of smart filter equipment will certainly be increased, and then increase natural gas cleaning cost, and the gas-liquid separation of Primordial Qi is only carried out by smart filter equipment, can not reliably realize thorough separation, portion of natural gas is caused to be misprinted waste.
Summary of the invention
The object of the invention is to: for above-mentioned the deficiencies in the prior art, a kind of redundancy running is provided, effectively can make solid, liquid, gas reliable separation in natural gas Primordial Qi, reduce the natural gas filter of cleaning cost.
The technical solution used in the present invention is: a kind of natural gas filter, and comprise the first identical filter mechanism of structure and the second filter mechanism, described filter also includes shunt conduit and bus dump; The two ends correspondence of described shunt conduit is connected to the first axial arranged filter mechanism and the front portion of the second filter mechanism, shunt conduit is provided with the air inlet of Primordial Qi, and the shunt conduit be provided with between the first stop valve and the second filter mechanism of the shunt conduit between this air inlet and the first filter mechanism is provided with the second stop valve; The two ends correspondence of described bus dump is connected to the rear portion of the first filter mechanism and the second filter mechanism, bus dump is provided with the gas outlet of purified gas, and the bus dump be provided with between the 3rd stop valve and the second filter mechanism of the bus dump between this gas outlet and the first filter mechanism is provided with the 4th stop valve.
Described filter mechanism is formed primarily of cylindrical shell, sparger and separator, the front end of described cylindrical shell is connected with three-way body, this three-way body is connected with flap type and shunt conduit respectively, the rear end of cylindrical shell is direct or be connected with bus dump by transition conduit, described sparger is axially inserted in cylindrical shell through flap type and three-way body, described separator is assemblied in the cylindrical shell at sparger rear, separator has some through flow holes.
Described sparger is formed with the chemical soap stick be filled in case primarily of the case of blind hole shape, and described case offers some through flow holes.
Through flow hole diameter on described sparger case is 3 ~ 10mm.
Described separator is filter plate, this filter plate offers the through flow hole that some lower diameter are less than upper diameter.
The through flow hole diameter of described filter plate bottom is 3 ~ 10mm; The through flow hole diameter on described filter plate top is 12 ~ 20mm.
Described cylindrical shell is that seamless steel pipe is shaping, and the front end of cylindrical shell and/or rear end are the cone-shaped structure of evagination.
Described cylindrical shell is provided with decontamination valve.
The invention has the beneficial effects as follows:
1. above-mentioned filter by two filter mechanisms effectively and define Redundancy Design reliably, two filter mechanisms can not only filter cleaning natural gas Primordial Qi simultaneously, and can also be formed each other " spare tyre ", thus guarantee that natural gas transmission pipeline normally runs, reliability is high, practical;
2. above-mentioned filter mechanism by arranging sparger and the separator of ad hoc structure in cylindrical shell, the natural gas Primordial Qi entered in cylindrical shell is bubbled consistently, foam collision and the action of stop froth breaking under inertia, thus in foaming with stop in froth breaking action solid impurity entrained by Primordial Qi is realized effectively and reliably filters, and then protect downstream fine filter equipment greatly, in foam crash-active, the gas-liquid of Primordial Qi has been made to carry out effectively and be reliably separated, alleviate the burden of downstream fine filter equipment, not only be conducive to the cleaning cost significantly reducing natural gas Primordial Qi, and the gas-liquid in Primordial Qi can be made to reach thorough separation as far as possible, reduce and misprint waste, good reliability.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, content of the present invention is further described.
Fig. 1 is a kind of structural representation of the present invention.
Fig. 2 is the structural representation of sparger case in Fig. 1.
Fig. 3 is the structural representation of separator in Fig. 1.
Code name implication in figure: the 1-the first filter mechanism; 101-flap type; 102-three-way body; 103-first reducer; 104-sparger; 105-cylindrical shell; 106-decontamination valve; 107-separator; 108-tail reducer; 109-transition conduit; 110,111-through flow hole; 112-case; 2-the second filter mechanism; 3-shunt conduit; 301-air inlet; 302-the first stop valve; 303-the second stop valve; 4-bus dump; 401-gas outlet; 402-the three stop valve; 403-the four stop valve.
Detailed description of the invention
See Fig. 1, Fig. 2 and Fig. 3: the present invention is used for natural gas Primordial Qi and filters, and with the solid, liquid, gas in isolated by filtration Primordial Qi, the present invention includes the first filter mechanism 1, second filter mechanism 2, shunt conduit 3 and bus dump 4.
Wherein, the first filter mechanism 1 is identical with the structure of the second filter mechanism 2, the existing structure only describing them for the first filter mechanism 1 in detail.
First filter mechanism 1 is formed primarily of cylindrical shell 105, sparger 104 and separator 107.Cylindrical shell 105 adopts seamless steel pipe shaping, and its draw ratio is generally 4 ~ 8:1.In order to realize use in throttling supercharging and be convenient to be connected with other conduit component, the front-end and back-end of cylindrical shell 105 are respectively the cone-shaped structure of evagination, reducer 103 headed by the front end of i.e. cylindrical shell 105, the rear end of cylindrical shell 105 is tail reducer 108, first reducer 103 and tail reducer 108 form with cylindrical shell 105 one or seal welding, the external diameter of corresponding sparger 104 is mated in the small-bore of first reducer 103, and corresponding following transition conduit 109 is mated in the small-bore of tail reducer 108.Be connected with three-way body 102 in the front end of aforementioned cylindrical shell 105, namely this three-way body 102 is connected to the small-bore end of first reducer 103; Be connected with the transition conduit 109 of curved shape in the rear end of cylindrical shell 105, namely this transition conduit 109 is connected to the small-bore end of tail reducer 108.The front end of aforementioned three-way body 102 is connected with flap type 101, and this flap type 101, three-way body 102 and cylindrical shell 105 should on the same axis, and this flap type 101 for loading sparger 104 in cylindrical shell 105; Three-way body 102, also for connecting shunt conduit 3, carries out isolated by filtration so that natural gas Primordial Qi is introduced cylindrical shell 105.Sparger 104 is formed with the chemical soap stick be filled in case 112 primarily of the case 112 of blind hole shape, the draw ratio of case 112 is generally 4 ~ 8:1, some through flow holes 110 are circumferentially offered at case 112, the diameter of each through flow hole 110 is 3 ~ 10mm, this value is too small to be unfavorable for Primordial Qi circulation and to bubble, this value excessive being unfavorable for bubbles, preferred median in aforementioned range; Sparger 104 is axially inserted in cylindrical shell 105 through flap type 101 and three-way body 102, and namely the dress of sparger 104 is got and realized by opening flap type 101.Separator 107 is filter plate (screen cloth can certainly be adopted to replace), and radially loading fits over the rear side of cylindrical shell 105 inside, and namely separator 107 need be in the cylindrical shell 105 at sparger 104 rear; The filter plate of aforementioned separator 107 offers some through flow holes 111, require that some bottoms through flow hole 111 diameter that filter plate is offered need be less than the diameter of some tops through flow hole 111, through flow hole 111 diameter of usual filter plate bottom is 3 ~ 10mm, such as 5mm, 7mm etc., this value is conducive to filtering solid of taking in Primordial Qi liquid, through flow hole 111 diameter on usual filter plate top is 12 ~ 20mm, such as 14mm, 17mm etc., this value is conducive to Primordial Qi foam and stops collision, and then discharges and through-flow gas.Conveniently filter mechanism cleaning, above-mentioned cylindrical shell 105 is provided with needle-valve, i.e. decontamination valve 106.
Shunt conduit 3 is three-way body structure actually, its two ends are respectively used to connection first stop valve 302 and the second stop valve 303, the three-way body 102 of the first filter mechanism 1 is docked again by the first stop valve 302, the three-way body of the second filter mechanism 2 is docked by the second stop valve 303, another interface of shunt conduit 3 is as air inlet 301, for connecting Primordial Qi conveyance conduit, namely the air inlet 301 of Primordial Qi is offered in the middle of shunt conduit 3, shunt conduit 3 between air inlet 301 and the first filter mechanism 1 is provided with the first stop valve 302, and the shunt conduit 3 between the second filter mechanism 2 is provided with the second stop valve 303.This arrangement of shunt conduit 3 between the first filter mechanism 1 and the second filter mechanism 2, chemical soap stick in Primordial Qi and sparger 104 is formed and fully washes away reaction, the bubble that reaction occurs produces and effectively collides separation under effect of inertia on separator 107.
Same, bus dump 4 is three-way body structure actually, its two ends are respectively used to connection the 3rd stop valve 402 and the 4th stop valve 403, (also can directly dock) tail end at the first filter mechanism 1 is docked by the transition conduit 109 of curved shape again by the 3rd stop valve 402, be docked at the tail end of the second filter mechanism 2 by the transition conduit of curved shape by the 4th stop valve 403, another interface of bus dump 4 is as gas outlet 401, for connecting purified gas (normally first product purified gas) conveyance conduit, namely on bus dump 4, be provided with the gas outlet 401 of purified gas, bus dump 4 between gas outlet 401 and the first filter mechanism 1 is provided with the 3rd stop valve 402, and the bus dump 4 between the second filter mechanism 2 is provided with the 4th stop valve 403.
Above-mentioned concrete technical scheme, only in order to the present invention to be described, is not intended to limit.Although with reference to above-mentioned concrete technical scheme to invention has been detailed description, those of ordinary skill in the art is to be understood that: it still can be modified to above-mentioned concrete technical scheme, or equivalent replacement is carried out to wherein portion of techniques feature; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of technical solution of the present invention.

Claims (7)

1. a natural gas filter, comprise identical the first filter mechanism (1) of structure and the second filter mechanism (2), described filter also includes shunt conduit (3) and bus dump (4); The two ends correspondence of described shunt conduit (3) is connected to axial arranged the first filter mechanism (1) and the front portion of the second filter mechanism (2), shunt conduit (3) is provided with the air inlet (301) of Primordial Qi, the shunt conduit (3) between this air inlet (301) and the first filter mechanism (1) be provided with the first stop valve (302), and the second filter mechanism (2) between shunt conduit (3) be provided with the second stop valve (303); The two ends correspondence of described bus dump (4) is connected to the rear portion of the first filter mechanism (1) and the second filter mechanism (2), bus dump (4) is provided with the gas outlet (401) of purified gas, the bus dump (4) between this gas outlet (401) and the first filter mechanism (1) be provided with the 3rd stop valve (402), and the second filter mechanism (2) between bus dump (4) be provided with the 4th stop valve (403); It is characterized in that: described filter mechanism is formed primarily of cylindrical shell, sparger and separator, the front end of described cylindrical shell is connected with three-way body, this three-way body is connected with flap type and shunt conduit (3) respectively, the rear end of cylindrical shell is direct or be connected with bus dump (4) by transition conduit, described sparger is axially inserted in cylindrical shell through flap type and three-way body, described separator is assemblied in the cylindrical shell at sparger rear, separator has some through flow holes.
2. natural gas filter according to claim 1, is characterized in that: described sparger is formed primarily of the case of blind hole shape and the chemical soap stick be filled in case, and described case offers some through flow holes.
3. natural gas filter according to claim 2, is characterized in that: the through flow hole diameter on described sparger case is 3 ~ 10mm.
4. natural gas filter according to claim 1, is characterized in that: described separator is filter plate, this filter plate offers the through flow hole that some lower diameter are less than upper diameter.
5. natural gas filter according to claim 4, is characterized in that: the through flow hole diameter of described filter plate bottom is 3 ~ 10mm; The through flow hole diameter on described filter plate top is 12 ~ 20mm.
6. natural gas filter according to claim 1, it is characterized in that: described cylindrical shell is that seamless steel pipe is shaping, the front end of cylindrical shell and/or rear end are the cone-shaped structure of evagination.
7. natural gas filter according to claim 1 or 6, is characterized in that: described cylindrical shell is provided with decontamination valve.
CN201410537002.4A 2014-10-13 2014-10-13 A kind of natural gas filter Active CN104258642B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107510994B (en) * 2015-10-16 2019-06-11 山东瑞祥环保科技有限公司 A kind of working method of the gas-liquid separator for desulfurization dust-removal system
CN105435491A (en) * 2015-12-18 2016-03-30 重庆欣雨压力容器制造有限责任公司 Solid antifoaming agent filling pry

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN200966963Y (en) * 2006-10-16 2007-10-31 上海微滤净化技术有限公司 Core for filtering and separating natural gas
CN201643932U (en) * 2010-01-22 2010-11-24 西安联合超滤净化设备有限公司 Device for separating heavy hydrocarbon in mixed gas
DE102011107621A1 (en) * 2010-07-05 2012-01-05 Uwe Athmann Preparing and purifying a product gas comprises thermochemical conversion of biomass in a reactor, conducting the produced, pollutant loaded product gas into a main gas treatment step, condensing the unwanted tars and filtering
CN104001381A (en) * 2014-05-21 2014-08-27 安徽新合大工程管理有限公司 Domestic air filter
CN204121894U (en) * 2014-10-13 2015-01-28 四川省德阳升发石油工具有限公司 A kind of natural gas filter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN200966963Y (en) * 2006-10-16 2007-10-31 上海微滤净化技术有限公司 Core for filtering and separating natural gas
CN201643932U (en) * 2010-01-22 2010-11-24 西安联合超滤净化设备有限公司 Device for separating heavy hydrocarbon in mixed gas
DE102011107621A1 (en) * 2010-07-05 2012-01-05 Uwe Athmann Preparing and purifying a product gas comprises thermochemical conversion of biomass in a reactor, conducting the produced, pollutant loaded product gas into a main gas treatment step, condensing the unwanted tars and filtering
CN104001381A (en) * 2014-05-21 2014-08-27 安徽新合大工程管理有限公司 Domestic air filter
CN204121894U (en) * 2014-10-13 2015-01-28 四川省德阳升发石油工具有限公司 A kind of natural gas filter

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