JPS59229072A - Gas compressor for well of natural gas - Google Patents

Gas compressor for well of natural gas

Info

Publication number
JPS59229072A
JPS59229072A JP10169883A JP10169883A JPS59229072A JP S59229072 A JPS59229072 A JP S59229072A JP 10169883 A JP10169883 A JP 10169883A JP 10169883 A JP10169883 A JP 10169883A JP S59229072 A JPS59229072 A JP S59229072A
Authority
JP
Japan
Prior art keywords
gas
compressor
drain
filter device
suction filter
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
JP10169883A
Other languages
Japanese (ja)
Inventor
Shoroku Suzuki
鈴木 荘六
Masahiro Ishii
雅浩 石井
Masaaki Sakurai
桜井 雅章
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.)
KACHI TEKKOSHO KK
TSUTSUI TOKUSHU KOGU SEISAKUSHO KK
Mitsui Toatsu Chemicals Inc
Original Assignee
KACHI TEKKOSHO KK
TSUTSUI TOKUSHU KOGU SEISAKUSHO KK
Mitsui Toatsu Chemicals Inc
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 KACHI TEKKOSHO KK, TSUTSUI TOKUSHU KOGU SEISAKUSHO KK, Mitsui Toatsu Chemicals Inc filed Critical KACHI TEKKOSHO KK
Priority to JP10169883A priority Critical patent/JPS59229072A/en
Publication of JPS59229072A publication Critical patent/JPS59229072A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B37/00Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
    • F04B37/10Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use
    • F04B37/18Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use for specific elastic fluids
    • F04B37/20Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use for specific elastic fluids for wet gases, e.g. wet air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • F04B39/16Filtration; Moisture separation

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Compressor (AREA)
  • Compressors, Vaccum Pumps And Other Relevant Systems (AREA)

Abstract

PURPOSE:To prevent the action of a water hammer, by equipping a drain pot of large capacity to the bottom part of a suction filter device. CONSTITUTION:The mist of submergence and the accompanying submergence at the time of sudden jet from a gas well are collectively removed by a demister 22, separately stored in a drain pot 24 of large capacity and continuously discharged by a trap 25. Gas, being allowed to flow into the first stage cylinder 26, is compressed by a piston 26a and cooled by an intercooler 27 further compressed by a piston 29a in the second stage cylinder 29 through a drain separator 28, and the gas is stored in a gas tank or the like.

Description

【発明の詳細な説明】 本発明は、天然ガス井戸より水溶性天然ガスを汲み上げ
るためのガスリフトポンプ用圧縮機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a compressor for a gas lift pump for pumping water-soluble natural gas from a natural gas well.

従来より、水溶性天然ガスは、一般に井戸よりガスリフ
トポンプによって地下かん木を汲み上げ、地上で圧力を
大気圧に解放することによって、かん水中に圧力によっ
て溶解している天然ガスを分離して採取されている。
Traditionally, water-soluble natural gas has been extracted by separating natural gas dissolved in brine under pressure by pumping up underground bushes from wells using gas lift pumps and releasing the pressure to atmospheric pressure above ground. ing.

前記ガスリフトポンプを作動するためには採取された天
然ガスを圧縮して使用するが、圧縮機の方は空気圧縮用
のものをそのま一使用しているのが実状である。しかし
水溶性天然ガスには特殊な性質があり、圧縮機の使用に
際し配慮をしないと、当然圧lii機の故障を招いたり
無駄にガス圧縮用エネルギーを消費したりする欠点を生
ずる。
In order to operate the gas lift pump, collected natural gas is compressed and used, but the reality is that the compressor used is for compressing air. However, water-soluble natural gas has special properties, and if care is not taken when using the compressor, it will inevitably cause malfunction of the compressor and waste energy for compressing the gas.

すなわち前記水溶性天然ガス中には微細な砂拳かん木の
ミストが同伴し、またガス井戸突噴時には、前記地上に
おける分離能力が間に合わず、かん木がそのま〜同伴す
る。従来の空気用圧縮機の構成系統を示す第1図におい
て、前記かん水が矢印Aの吸込側から入り、かん木が圧
縮機内で木槌作用をおこして、図示しないクランク軸折
損等の車数を発生する。また水溶性天然ガスは主成分が
メタン(CH,)であり、空気より大きな比熱を有する
。従って従来の空気用インタークーラー11の冷却能力
を 1.5倍以上に大きくしないと、前記圧縮ガスの冷
却が十分に行えず、ガス圧縮用の無駄なエネルギーを消
費し、その上ガス温度上昇による圧縮機の故障を誘発す
る。さらに水溶性天然カス中には、1%内外の炭酸ガス
(CO2)を含有しており、水との共存条件下で溶解し
て炭酸となる。金属材料は一般に酸に腐蝕されるので、
冷却によってドレンを発生する前記インタークーラー1
1の鉄製等のクーラーチューブ等の冷却面11’aは、
肉厚も薄く炭酸の影響を受けて腐蝕欠陥を生じやすい。
That is, the water-soluble natural gas is accompanied by a fine mist of sandy shrubs, and when a gas well blows up, the above-ground separation ability is not in time, and the shrubs are entrained as they are. In Figure 1, which shows the structural system of a conventional air compressor, the brine enters from the suction side indicated by arrow A, and the shrubs cause a mallet action within the compressor, resulting in a number of cars with broken crankshafts (not shown). Occur. Furthermore, water-soluble natural gas has methane (CH,) as its main component and has a higher specific heat than air. Therefore, unless the cooling capacity of the conventional air intercooler 11 is increased by 1.5 times or more, the compressed gas cannot be cooled sufficiently, wasted energy for gas compression is consumed, and furthermore, the compression due to the rise in gas temperature increases. cause machine failure. Furthermore, the water-soluble natural scum contains around 1% carbon dioxide gas (CO2), which dissolves to form carbonic acid under conditions of coexistence with water. Metal materials are generally corroded by acids, so
The intercooler 1 generates drain by cooling.
The cooling surface 11'a of the cooler tube made of iron or the like in No. 1 is
The wall thickness is also thin and susceptible to corrosion defects due to the effects of carbonic acid.

また水溶性天然ガスの主成分である前記メタン(CH,
)は爆発性があり危険である。
In addition, the methane (CH,
) are explosive and dangerous.

本発明は上述の諸問題を克服して、水溶性天然ガスが圧
力によって溶解している地下かん木を井戸から汲み上げ
る為iこ、ガスリフトポンプとして作動させる圧縮ガス
を作る、新規のガス圧縮機を提供することを目的とする
The present invention overcomes the above-mentioned problems and provides a novel gas compressor for pumping underground shrubs from wells in which water-soluble natural gas is dissolved under pressure, producing compressed gas that operates as a gas lift pump. The purpose is to provide.

すなわち、水溶性天然ガス汲み上げ用ガス圧縮機におい
て、ガス吸込側にデミスタ−を内臓する吸込フィルター
装置があり、その下部に比較的大容量のドレンポットを
装着している。吸込フィルター装置の下流に順次、ピス
トンを内臓する1段シリンダー・インタークーラ−9ド
レンセパレーター・ピストン内臓の2段シリンターと配
設され、クランクケースと吸込フィルター装置の中間に
逆止弁又は調圧弁を設けて、本圧縮機は構成されている
That is, in a gas compressor for pumping water-soluble natural gas, there is a suction filter device containing a demister on the gas suction side, and a relatively large-capacity drain pot is installed at the bottom of the suction filter device. A one-stage cylinder with a built-in piston, an intercooler, a nine-drain separator, and a two-stage cylinder with a built-in piston are installed downstream of the suction filter device, and a check valve or pressure regulating valve is installed between the crankcase and the suction filter device. The present compressor is configured as follows.

以下、本発明に係わるガス圧lii機の実施例を、図面
を参照して説明する。第2図は、本実施例を説明する為
の構成系統図であり、第3図は、ピストンからクランク
ケース内へのもれガス対策説明の為の構成系統図である
。第2図において、ガス圧縮機21のガス吸込(矢印B
)側(図では左側)にステンレスデミスタ−22を内臓
する吸込フィルター装置23があり、吸込フィルター装
置23の下部にドレンポット24、下方部にトラップ2
5がある。    ′吸込フィルター装置23の下流(
図では右方)に順次、1段シリンダー26φ酎食材料製
冷却面27aを有するインタークーラー270ドレンセ
パレーター28・2段シリンダー29がある。第3図に
おいては、クランクケース31内にクランク軸32があ
り、クランクケース31から吸込フィルター装置23内
の吸込側ヘガスが一方的に流れるように(図では左方へ
)、両者の中間に逆止弁又は調圧弁33を設けである。
EMBODIMENT OF THE INVENTION Hereinafter, an embodiment of a gas pressure LII machine according to the present invention will be described with reference to the drawings. FIG. 2 is a structural diagram for explaining this embodiment, and FIG. 3 is a structural diagram for explaining measures against gas leaking from the piston into the crankcase. In FIG. 2, the gas suction of the gas compressor 21 (arrow B
) side (left side in the figure) is a suction filter device 23 containing a stainless steel demister 22, a drain pot 24 at the bottom of the suction filter device 23, and a trap 2 at the bottom.
There are 5. 'Downstream of the suction filter device 23 (
On the right side in the figure, there are an intercooler 270, a drain separator 28, and a second cylinder 29, which have a first-stage cylinder 26φ and a cooling surface 27a made of alcoholic beverage material. In FIG. 3, there is a crankshaft 32 inside the crankcase 31, and the gas flows unilaterally (to the left in the figure) from the crankcase 31 to the suction side of the suction filter device 23, and vice versa between the two. A stop valve or pressure regulating valve 33 is provided.

次にその作用について説明すると、第2図において吸込
フィルター装置23内の吸込側から入る天然ガス中に含
まれている前記微細な砂・かん木のミストや、前記ガス
井戸突噴時の同伴かん木を、デミスタ−22により捕集
除去し、吸込フィルター装置23内の下部に前記空気用
ガス圧縮機のドレンポットより大容量のドレンポット2
4に分離貯蔵し、トラップ25により連続排出する。次
にガスは1段シリンダー26内に入りピストン28aに
より圧縮され、十分な冷却能力を有するインタークーラ
ー27で冷却されて、ドレンセパレーター28ヲ介して
2段シリンダー2θ内でピストン29aにより更に圧縮
され、圧縮ガスとして(以下の諸装置は図示しない)ガ
ス槽等に貯えられる。さらに圧縮ガスは配管を介して井
戸底に送られ、圧縮ガスの気泡により、管底で接続して
いる別の太目の管を介して地下かん木を地上へ汲′み上
げるガスリットポンプの作用を行う。
Next, to explain its effect, as shown in FIG. The wood is collected and removed by a demister 22, and a drain pot 2 with a larger capacity than the drain pot of the air gas compressor is installed in the lower part of the suction filter device 23.
4 and are stored separately and continuously discharged through a trap 25. Next, the gas enters the first stage cylinder 26, is compressed by the piston 28a, is cooled by the intercooler 27 having sufficient cooling capacity, is further compressed by the piston 29a in the second stage cylinder 2θ via the drain separator 28, and is compressed. It is stored as a gas (the following devices are not shown) in a gas tank or the like. Furthermore, the compressed gas is sent to the bottom of the well via piping, and the bubbles of the compressed gas act as a gas slit pump to pump underground shrubs to the surface through another thick pipe connected at the bottom of the pipe. I do.

次にその効果について説明すると、第2図および第3図
において、前記デミスタ−22がドレンポット24を比
較的大容量としてドレンを分離し、トラップ25により
天然ガス中のかん水等と共に連続排出を行わせることに
より、圧縮機内への吸込かん木に基づく木槌作用による
、圧縮機21の前記クランク軸32の折損等の事故を防
止できる効果を奏する。さらに微細な砂やミストを分離
することにより、シリンダー弁の破損摩耗等のトラブル
を防止する。
Next, to explain the effect, in FIGS. 2 and 3, the demister 22 separates the drain from the drain pot 24 with a relatively large capacity, and the trap 25 continuously discharges the drain along with brine etc. in the natural gas. By doing so, it is possible to prevent accidents such as breakage of the crankshaft 32 of the compressor 21 due to the mallet action caused by suction shrubs into the compressor. Furthermore, by separating fine sand and mist, troubles such as damage and wear of cylinder valves are prevented.

また前記インタークーラー27の冷却面2?aの冷却能
力が従来の空気用インタークーラー冷却面の1.5倍以
上あるので、省エネルギーでガスを圧縮することができ
ると共にカス温度上昇による圧縮機の故障誘発を防ぐ効
果を奏する。またインタークーラー27の材質をステン
レス鋼等耐食材才′1とし、望ましくは弁ポート部をド
レン溜りの無い形状とすることにより天然カス中の炭酸
カス(CO))か水に溶解して生ずる炭酸による腐蝕を
防止できる。さらに天然ガス中の主成分たるメタン(C
ル)が前記ピストン26aおよび29aの圧縮により、
前記クランクケース31内にもれてきてもクランクケー
ス31を密閉して外部へもらさず、かつ前記逆止弁又は
調圧弁33を介して前記吸込フィルター装置23内の吸
込側へ戻す循環路を設けであるので、メタン(CH,)
の外部へのもれによる爆発事故を防ぎ、資源の有効利用
を図る効果も奏する。
Also, the cooling surface 2 of the intercooler 27? Since the cooling capacity of a is more than 1.5 times that of the conventional air intercooler cooling surface, it is possible to compress gas with energy savings, and it also has the effect of preventing compressor failure due to a rise in waste temperature. In addition, the material of the intercooler 27 is made of corrosion-resistant material such as stainless steel, and the valve port part is preferably shaped without a drain reservoir, so that carbon dioxide (CO) in natural scum or carbonic acid generated by dissolving in water can be used. Can prevent corrosion. Furthermore, methane (C) is the main component of natural gas.
) due to the compression of the pistons 26a and 29a,
A circulation path is provided that seals the crankcase 31 so that even if it leaks into the crankcase 31, it does not leak outside, and returns it to the suction side of the suction filter device 23 via the check valve or pressure regulating valve 33. Therefore, methane (CH,)
It also has the effect of preventing explosion accidents due to leakage to the outside and promoting effective use of resources.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、従来のガス圧縮機の構成系統図。 第2図は、本発明の実施例の構成系統図。 第3図は、本実施例の、もれガス対策用構成系統図。 21・・・ガス圧縮機、22・・・デミスタ−123・
・・吸込フィルター装置、24・・・ドレンポット、2
6a・・・1段圧縮用ビス)・ン、27・・・インター
クーラー29a・・・2段圧縮用ピストン、31・・・
クランクケース、33・・・逆止弁又は調圧弁。 特許出願人 三井東圧化学株式会社 株式会社 加地鉄工所
FIG. 1 is a structural diagram of a conventional gas compressor. FIG. 2 is a structural diagram of an embodiment of the present invention. FIG. 3 is a structural diagram for leakage gas countermeasures in this embodiment. 21... Gas compressor, 22... Demister-123.
...Suction filter device, 24...Drain pot, 2
6a... 1st stage compression screw), 27... Intercooler 29a... 2nd stage compression piston, 31...
Crank case, 33... Check valve or pressure regulating valve. Patent applicant Mitsui Toatsu Chemical Co., Ltd. Kaji Iron Works Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 水溶性天然ガス汲み上げ用ガス圧縮機において、吸込フ
ィルター装置内にミスト除去用のデミスタ−を設け、該
吸込フィルター装置内の下部にドレン除去用の比較的大
容量のドレンボットを設け、同容−着の空気用圧縮機よ
り大きな冷却能力をもつ耐食材料製のインタークーラー
を有し、ピストンからクランクケースへの洩出ガスを該
吸込フィルター装置内の吸込側にリサイクルさせる循環
路を設けて、該循環路に逆止弁又は調圧弁を具えたこと
を特徴とする天然ガス井戸用ガス圧縮機。
In a gas compressor for pumping water-soluble natural gas, a demister for removing mist is provided in the suction filter device, and a relatively large-capacity drain bot for removing drain is provided in the lower part of the suction filter device. It has an intercooler made of corrosion-resistant material that has a larger cooling capacity than the air compressor of A gas compressor for a natural gas well, characterized in that the gas compressor is equipped with a check valve or a pressure regulating valve.
JP10169883A 1983-06-09 1983-06-09 Gas compressor for well of natural gas Pending JPS59229072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10169883A JPS59229072A (en) 1983-06-09 1983-06-09 Gas compressor for well of natural gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10169883A JPS59229072A (en) 1983-06-09 1983-06-09 Gas compressor for well of natural gas

Publications (1)

Publication Number Publication Date
JPS59229072A true JPS59229072A (en) 1984-12-22

Family

ID=14307541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10169883A Pending JPS59229072A (en) 1983-06-09 1983-06-09 Gas compressor for well of natural gas

Country Status (1)

Country Link
JP (1) JPS59229072A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5131825A (en) * 1990-03-27 1992-07-21 Leybold Aktiengesellschaft Multi-stage vacuum pump with reaction chamber between stages
US5173041A (en) * 1990-09-21 1992-12-22 Ebara Corporation Multistage vacuum pump with interstage solid material collector and cooling coils
JPWO2016006092A1 (en) * 2014-07-11 2017-04-27 株式会社日立製作所 Compressor
CN112146271A (en) * 2020-09-24 2020-12-29 中海石油(中国)有限公司 Ultrahigh pressure heat exchange system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5131825A (en) * 1990-03-27 1992-07-21 Leybold Aktiengesellschaft Multi-stage vacuum pump with reaction chamber between stages
US5173041A (en) * 1990-09-21 1992-12-22 Ebara Corporation Multistage vacuum pump with interstage solid material collector and cooling coils
JPWO2016006092A1 (en) * 2014-07-11 2017-04-27 株式会社日立製作所 Compressor
CN112146271A (en) * 2020-09-24 2020-12-29 中海石油(中国)有限公司 Ultrahigh pressure heat exchange system
CN112146271B (en) * 2020-09-24 2022-02-25 中海石油(中国)有限公司 Ultrahigh pressure heat exchange system

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