JP2003042397A - Gas usage method and device - Google Patents
Gas usage method and deviceInfo
- Publication number
- JP2003042397A JP2003042397A JP2001226036A JP2001226036A JP2003042397A JP 2003042397 A JP2003042397 A JP 2003042397A JP 2001226036 A JP2001226036 A JP 2001226036A JP 2001226036 A JP2001226036 A JP 2001226036A JP 2003042397 A JP2003042397 A JP 2003042397A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- pipe
- compressor
- pressure
- storage means
- 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.)
- Granted
Links
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ガスを圧縮する圧
縮機、このガスを貯蔵する貯蔵手段及び前記圧縮機と貯
蔵手段の間でガスを輸送するための配管を有するガスの
貯蔵設備において、前記配管の途中で分岐配管を設け、
この分岐部分と前記ガス貯蔵手段の間の前記配管中に背
圧手段を設けるとともに、前記分岐配管中に減圧手段を
設け、これによって減圧されているが比較的高い圧力の
ガスを消費設備に供給する、ガスの利用方法及び装置に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas storage facility having a compressor for compressing gas, storage means for storing the gas, and piping for transporting the gas between the compressor and the storage means. Provide a branch pipe in the middle of the pipe,
A back pressure means is provided in the pipe between the branch portion and the gas storage means, and a decompression means is provided in the branch pipe to supply a gas having a relatively high pressure, which is decompressed by the decompression means. And a gas utilization method and device.
【0002】[0002]
【従来の技術】下水処理場、食品工場、ビール製造工
場、家畜の飼育場等で生じる有機性廃棄物を生物学的に
処理すると、メタン、二酸化炭素、硫化水素、チオー
ル、トルエン、シロキサン等からなるバイオガスが発生
する。近年かかるバイオガスをエネルギー源として有効
利用するために、バイオガスを吸着貯蔵する方法につい
ての研究が盛んである。2. Description of the Related Art Biological treatment of organic waste generated in sewage treatment plants, food factories, beer factories, livestock farms produces methane, carbon dioxide, hydrogen sulfide, thiols, toluene, siloxanes, etc. Biogas is generated. In recent years, research has been actively conducted on a method of adsorbing and storing biogas in order to effectively use such biogas as an energy source.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記の
ような貯蔵方法の他に、バイオガスをどのように利用す
るかについてはあまり研究がなされていない。本発明
は、バイオガスを包含するガス一般について、新しい利
用の仕方を提案しようとするものである。However, other than the above storage method, much research has not been done on how to use biogas. The present invention seeks to propose a new usage method for general gases including biogas.
【0004】[0004]
【課題を解決するための手段】本発明は、ガスを圧縮す
る圧縮機、このガスを貯蔵する貯蔵手段及び前記圧縮機
と貯蔵手段の間でガスを輸送するための配管を有するガ
スの貯蔵設備において、前記配管の途中で分岐配管を設
け、この分岐部分と前記ガス貯蔵手段の間の前記配管中
に背圧手段を設けるとともに、前記分岐配管中に減圧手
段を設け、これによって減圧されたガスを消費設備に供
給するガスの利用装置に関する。本発明はまた、かかる
ガスの利用装置において、前記消費設備が1基又は複数
基のガスタービン又はマイクロガスタービンであり、そ
のガスを燃料として発電するガスの利用装置を提供する
ものである。本発明はまた、かかるガスの利用装置にお
いて、前記背圧手段が背圧弁又はオリフィスであるガス
の利用装置を提供するものである。本発明はまた、かか
るガスの利用装置において、前記減圧手段が減圧弁又は
オリフィスであるガスの利用装置を提供するものであ
る。本発明はまた、かかるガスの利用装置において、前
記ガスがメタンを主成分とするガスであるガスの利用装
置を提供するものである。本発明はまた、かかるガスの
利用装置において、前記メタンを主成分とするガスが有
機物の生物学的処理によって発生するバイオガスに由来
するものであり、前記圧縮機の前に脱硫設備を有するガ
スの利用装置を提供するものである。本発明はまた、か
かるガスの利用装置において、前記貯蔵手段が吸着式ガ
スホルダーであるガスの利用装置を提供するものであ
る。本発明はまた、かかるガスの利用装置において、前
記圧縮機と貯蔵手段の間の配管又は分岐配管の中にガス
中の水分をとり除く除湿機構を有するガスの利用装置を
提供するものである。本発明はまた、かかるガスの利用
装置において、前記除湿機構の下流に、メタン、硫黄化
合物、二酸化炭素及び水分以外のガスを除く装置を有す
るガスの利用装置を提供するものである。SUMMARY OF THE INVENTION The present invention is a gas storage facility having a compressor for compressing gas, a storage means for storing the gas, and piping for transporting the gas between the compressor and the storage means. In the above, a branch pipe is provided in the middle of the pipe, a back pressure means is provided in the pipe between the branch portion and the gas storage means, and a pressure reducing means is provided in the branch pipe, thereby reducing the gas pressure. The present invention relates to a gas utilization device for supplying gas to consumption equipment. The present invention also provides such a gas utilization device in which the consumption facility is one or a plurality of gas turbines or micro gas turbines, and which uses the gas as fuel for power generation. The present invention also provides such a gas utilization device in which the back pressure means is a back pressure valve or an orifice. The present invention also provides such a gas utilization device in which the decompression means is a decompression valve or an orifice. The present invention also provides, in such a gas utilization device, a gas utilization device in which the gas is a gas containing methane as a main component. The present invention is also a gas utilization apparatus, wherein the gas containing methane as a main component is derived from biogas generated by a biological treatment of an organic matter, and a gas having a desulfurization facility in front of the compressor. Is provided. The present invention also provides such a gas utilization device, wherein the storage means is an adsorption gas holder. The present invention also provides, in such a gas utilization device, a gas utilization device having a dehumidification mechanism for removing moisture in the gas in a pipe or a branch pipe between the compressor and the storage means. The present invention also provides, in such a gas utilization device, a gas utilization device having a device for removing gases other than methane, sulfur compounds, carbon dioxide, and moisture downstream of the dehumidifying mechanism.
【0005】本発明はまた、上記ガス利用装置を用いる
ガスの利用方法であって、前記ガス圧縮機により前記圧
縮機と前記背圧手段の間の配管及び前記分岐部分と前記
減圧手段の間の分岐配管中のガスの圧力を高め、次いで
前記減圧手段によりこのガスを減圧し、減圧後のガス圧
が前記貯蔵手段における圧力よりも高いガスを消費設備
に供給することを包含するガスの利用方法を提供するも
のである。The present invention is also a method of utilizing gas using the above-mentioned gas utilization device, wherein the gas compressor is used to connect the pipe between the compressor and the back pressure means and between the branch portion and the pressure reducing means. A method of using a gas, which comprises increasing the pressure of a gas in a branch pipe, then reducing the pressure of the gas by the decompression means, and supplying a gas whose decompressed gas pressure is higher than the pressure in the storage means to a consumption facility. Is provided.
【0006】上記背圧手段を設けることにより、圧縮手
段と背圧手段の間の圧力を増し、前記貯蔵手段中のガス
圧よりも高いガス圧を得ることができる。この比較的高
い圧力を用いて、前記貯蔵手段における比較的低いガス
圧では運転できない消費設備を運転することが可能にな
る。このような消費設備としては、ガスタービンやマイ
クロガスタービンが存在しうる。By providing the back pressure means, the pressure between the compression means and the back pressure means can be increased, and a gas pressure higher than the gas pressure in the storage means can be obtained. This relatively high pressure makes it possible to operate consuming equipment which cannot be operated at relatively low gas pressures in the storage means. A gas turbine or a micro gas turbine may be present as such a consumption facility.
【0007】[0007]
【発明の実施の形態】前記背圧手段としては、背圧弁又
はオリフィスを用いることができる。A back pressure valve or an orifice may be used as the back pressure means.
【0008】前記減圧手段としては、減圧弁又はオリフ
ィスを用いることができる。A pressure reducing valve or an orifice can be used as the pressure reducing means.
【0009】前記ガスはメタンを主成分とするガスが好
ましい。このメタンを主成分とするガスは、有機物の生
物学的処理によって発生するバイオガスに由来するもの
であることが好ましい。ここにいう「由来する」とは、
そのままでもよいし、また好ましくは脱硫及び脱二酸化
炭素を行ったものである。The gas preferably contains methane as a main component. The gas containing methane as a main component is preferably derived from biogas generated by biological treatment of organic substances. "Derived from" here means
It may be used as it is, or preferably desulfurized and decarbonated.
【0010】このバイオガスは、消化ガス及びランドフ
ィルガスを包含する。このバイオガスは、メタンを主成
分とし、二酸化炭素、硫化水素やチオール等の硫黄化合
物、水素ガス、トルエン、シロキサン等を含有するもの
である。前記硫黄化合物は、装置を腐食する傾向を有す
るから予め除くのが好ましい。その脱硫方法としては、
乾式と湿式がある。乾式脱硫法には成形脱硫剤方式が多
く使用され、脱硫剤としては、鉄粉、粘土等でペレット
状にした成形脱硫剤等が用いられる。湿式脱硫法では、
水洗浄式、アルカリ洗浄式及び薬液再生式等がある。The biogas includes digestive gas and landfill gas. This biogas contains methane as a main component and contains carbon dioxide, sulfur compounds such as hydrogen sulfide and thiol, hydrogen gas, toluene, siloxane and the like. Since the sulfur compound has a tendency to corrode the device, it is preferably removed in advance. As the desulfurization method,
There are dry type and wet type. A molding desulfurization agent system is often used in the dry desulfurization method, and as the desulfurization agent, a molding desulfurization agent pelletized with iron powder, clay or the like is used. In the wet desulfurization method,
There are water washing type, alkaline washing type, chemical regenerating type and the like.
【0011】前記バイオガスには、二酸化炭素が多量に
含まれ(通常約40容量%)、これはバイオガスの燃料
としての単位体積当たりの発熱量を下げ、ガス輸送及び
ガス貯蔵を非効率にするから、除くのが好ましい。その
方法としては、活性炭、ゼオライト、金属酸化物等の二
酸化炭素吸着剤を充填した吸着塔や、気体分離膜や、多
孔性中空糸膜などを有するものが挙げられる。The biogas contains a large amount of carbon dioxide (usually about 40% by volume), which lowers the calorific value per unit volume of biogas as a fuel, making gas transportation and gas storage inefficient. Therefore, it is preferable to remove it. Examples of the method include those having an adsorption tower filled with a carbon dioxide adsorbent such as activated carbon, zeolite, or a metal oxide, a gas separation membrane, or a porous hollow fiber membrane.
【0012】前記貯蔵手段は、吸着式ガスホルダーであ
ることが好ましい。これによってガスの貯蔵を低圧で多
量にすることができるからである。この吸着剤の例とし
ては、活性炭、人工ゼオライト、天然ゼオライト、シリ
カゲル、有機金属錯体(フマル酸銅、テレフタル酸銅
等)が挙げられる。The storage means is preferably an adsorption type gas holder. This makes it possible to store a large amount of gas at low pressure. Examples of this adsorbent include activated carbon, artificial zeolite, natural zeolite, silica gel, organometallic complexes (copper fumarate, copper terephthalate, etc.).
【0013】前記圧縮機と貯蔵手段の間の配管又は分岐
配管の中にガス中の水分を取り除く除湿機構が存在する
ことが好ましい。この除湿機構は前記分岐部分と、圧縮
機、貯蔵手段又は減圧手段との間のどこの置いてもかま
わない。この水分は前記貯蔵手段中の吸着剤の吸着性能
を低下させるおそれがあり、また、配管や消費設備を腐
食させるおそれがあるからである。It is preferable that a dehumidifying mechanism for removing water in the gas is present in the pipe or the branch pipe between the compressor and the storage means. This dehumidification mechanism may be located anywhere between the branch and the compressor, storage means or decompression means. This is because this moisture may reduce the adsorption performance of the adsorbent in the storage means and may corrode the pipes and the consumption equipment.
【0014】前記除湿機構の下流には、メタン、硫黄化
合物、二酸化炭素及び水分以外のガス、例えばトルエン
やシロキサンを除く装置を置くのが好ましい。これら
は、活性炭で吸着除去することができる。A device for removing gases other than methane, sulfur compounds, carbon dioxide and water such as toluene and siloxane is preferably placed downstream of the dehumidifying mechanism. These can be adsorbed and removed with activated carbon.
【0015】以下に図面に本発明の一例を挙げて説明を
する。図1において、1は消化槽、2は脱硫塔、3は脱
二酸化炭素装置、4は低圧ガスホルダーである。消化槽
1は、これに投入する原料の種類が一定せず、その供給
量も一定しないから、生成するバイオガスの量も一定し
ない。従って、低圧ガスホルダー4は、可変容量式のも
のがよい。5は、このガスホルダーからの利用設備への
配管を示す。10は脱硫塔である。この図において、点
線で描かれているのは、必ずしも必要がないという意味
である。脱硫塔2では、硫化水素等の硫黄化合物含量が
通常約1〜10ppmである。脱硫塔10ではガス中の硫
化水素等の硫黄化合物含量が通常約1ppm未満となるよ
うに脱硫する。硫化水素等の硫黄化合物含量が通常約1
〜10ppmの程度でこのガスが使用可能であれば、脱硫
塔10は必要ない。コンプレッサー11を腐食から守り
長期使用したいときは、脱硫塔10を設けるのが好まし
い。低圧ガスホルダーの貯留量により、このコンプレッ
サー11の運転を制御する。12は除湿機構であり、1
3はメタン等以外のトルエンやシロキサンガス等のその
他のガス成分の除去装置である。An example of the present invention will be described below with reference to the drawings. In FIG. 1, 1 is a digestion tank, 2 is a desulfurization tower, 3 is a carbon dioxide removal device, and 4 is a low pressure gas holder. In the digestion tank 1, since the types of raw materials to be charged into the digestion tank 1 are not constant and the supply amount thereof is not constant, the amount of biogas produced is also not constant. Therefore, the low pressure gas holder 4 is preferably a variable capacity type. Reference numeral 5 shows a pipe from the gas holder to the facility used. 10 is a desulfurization tower. In this figure, what is drawn with a dotted line means that it is not always necessary. In the desulfurization tower 2, the content of sulfur compounds such as hydrogen sulfide is usually about 1 to 10 ppm. In the desulfurization tower 10, desulfurization is performed so that the content of sulfur compounds such as hydrogen sulfide in the gas is usually less than about 1 ppm. The content of sulfur compounds such as hydrogen sulfide is usually about 1
If this gas can be used in the range of about 10 ppm, the desulfurization tower 10 is not necessary. When desiring to protect the compressor 11 from corrosion and to use it for a long period of time, it is preferable to provide the desulfurization tower 10. The operation of the compressor 11 is controlled by the storage amount of the low pressure gas holder. 12 is a dehumidifying mechanism, and 1
3 is a device for removing other gas components such as toluene and siloxane gas other than methane.
【0016】14は背圧弁であり、15は吸着式ガスホ
ルダーである。このガスホルダー15中のガス圧は、例
えばゲージ圧200kPa である。16はこのガスホルダ
ーからの利用設備への配管を示す。この利用設備として
は、温水ボイラー、ガスエンジン(発電設備)、LPG
ボンベへの充填による利用設備、一般家庭への配管での
配給による消費等がある。21は減圧弁であり、22は
マイクロガスタービン(本発明でいう消費設備)であ
る。このマイクロガスタービンの代わりにガスタービン
を使用してもよい。このマイクロガスタービン22に供
給するバイオガスの圧力は、例えば300kPa である。
前記背圧弁のような背圧手段を設けることにより、圧縮
機と貯蔵手段の間の配管の間の圧力を高めることがで
き、更に減圧手段を設けることにより消費設備に適した
圧力にすることができる。本発明によれば、このよう
に、ガスホルダー15の中のガス圧よりも高い圧力の消
費設備でもバイオガス等の燃料ガスの使用が可能にな
る。Reference numeral 14 is a back pressure valve, and 15 is an adsorption type gas holder. The gas pressure in the gas holder 15 is, for example, a gauge pressure of 200 kPa. Reference numeral 16 denotes a pipe from the gas holder to the facility used. Facilities for this use include hot water boilers, gas engines (power generation facilities), and LPG.
There are equipment used for filling cylinders and consumption by distribution to households by piping. Reference numeral 21 is a pressure reducing valve, and 22 is a micro gas turbine (consumption facility in the present invention). A gas turbine may be used instead of the micro gas turbine. The pressure of biogas supplied to the micro gas turbine 22 is, for example, 300 kPa.
By providing the back pressure means such as the back pressure valve, the pressure between the pipes between the compressor and the storage means can be increased, and by further providing the pressure reduction means, the pressure suitable for the consumption equipment can be obtained. it can. According to the present invention, as described above, it becomes possible to use the fuel gas such as biogas even in a consumption facility having a pressure higher than the gas pressure in the gas holder 15.
【0017】このマイクロガスタービンの排ガスの顕熱
を利用して、蒸気又は温水を製造することができる。ま
た、得られた蒸気又は温水で、消化槽1を加温すること
ができる。また、マイクロガスタービン等で得られた電
力を処理場内で利用することができる。例えば、曝気槽
のブロワー、消化ガス供給用のガス圧縮機などの電力と
して利用できる。Steam or hot water can be produced by utilizing the sensible heat of the exhaust gas of the micro gas turbine. Moreover, the digestion tank 1 can be heated with the obtained steam or hot water. Further, the electric power obtained by the micro gas turbine or the like can be used in the treatment plant. For example, it can be used as electric power for a blower of an aeration tank, a gas compressor for supplying digestion gas, and the like.
【0018】[0018]
【発明の効果】本発明によれば、ガスを圧縮して貯蔵容
器に貯蔵し、これから消費設備に利用するだけでなく、
このガス貯蔵容器よりも高い圧力のガスを要求する消費
設備にも、簡単にガスを供給することができる。According to the present invention, not only is gas compressed and stored in a storage container and then used for consumption equipment,
The gas can be easily supplied to the consumption facility that requires the gas at a pressure higher than that of the gas storage container.
【図1】 本発明のガス利用装置の一実施形態を示すフ
ローシートである。FIG. 1 is a flow sheet showing an embodiment of a gas utilization apparatus of the present invention.
1…消化槽 2…脱硫塔 3…脱二酸化炭素塔 4…低圧ガスホルダー 5…利用設備への配管 10…脱硫塔 11…コンプレッサー 12…除湿機構 13…その他のガス成分の除去装置 14…背圧弁 15…吸着式ガスホルダー 16…利用設備への配管 21…減圧弁 22…マイクロガスタービン 1 ... digestion tank 2 ... Desulfurization tower 3 ... Decarbonization tower 4 ... Low pressure gas holder 5 ... Piping to the equipment used 10 ... Desulfurization tower 11 ... Compressor 12 ... Dehumidifying mechanism 13 ... Equipment for removing other gas components 14 ... Back pressure valve 15 ... Adsorption type gas holder 16… Piping to equipment used 21 ... Pressure reducing valve 22 ... Micro gas turbine
Claims (10)
する貯蔵手段及び前記圧縮機と貯蔵手段の間でガスを輸
送するための配管を有するガスの貯蔵設備において、前
記配管の途中で分岐配管を設け、この分岐部分と前記ガ
ス貯蔵手段の間の前記配管中に背圧手段を設けるととも
に、前記分岐配管中に減圧手段を設け、これによって減
圧されたガスを消費設備に供給するガスの利用装置。1. A gas storage facility comprising a compressor for compressing gas, a storage means for storing the gas, and a pipe for transporting the gas between the compressor and the storage means, and a branch in the middle of the pipe. A pipe is provided, and a back pressure unit is provided in the pipe between the branched portion and the gas storage unit, and a decompression unit is provided in the branch pipe so that the gas decompressed by the gas is supplied to the consumption facility. Utilization device.
ービン又はマイクロガスタービンであり、そのガスを燃
料として発電するものである請求項1に記載のガスの利
用装置。2. The gas utilization apparatus according to claim 1, wherein the consumption facility is one or a plurality of gas turbines or micro gas turbines, and the gas is used as fuel to generate electricity.
ある請求項1又は2に記載のガスの利用装置。3. The gas utilization apparatus according to claim 1, wherein the back pressure means is a back pressure valve or an orifice.
ある請求項1〜3のいずれかに記載のガスの利用装置。4. The gas utilization apparatus according to claim 1, wherein the pressure reducing means is a pressure reducing valve or an orifice.
ある請求項1〜4のいずれかに記載のガスの利用装置。5. The gas utilization apparatus according to claim 1, wherein the gas is a gas containing methane as a main component.
の生物学的処理によって発生するバイオガスに由来する
ものであり、前記圧縮機の前に脱硫設備を有する請求項
5に記載のガスの利用装置。6. The gas according to claim 5, wherein the gas containing methane as a main component is derived from biogas generated by biological treatment of an organic matter, and a desulfurization facility is provided in front of the compressor. Utilization device.
る請求項1〜6のいずれかに記載のガスの利用装置。7. The gas utilization apparatus according to claim 1, wherein the storage means is an adsorption type gas holder.
岐配管の中にガス中の水分を取り除く除湿機構を有する
請求項1〜7のいずれかに記載のガスの利用装置。8. The gas utilization device according to claim 1, further comprising a dehumidification mechanism for removing water in the gas, in a pipe or a branch pipe between the compressor and the storage means.
合物、二酸化炭素及び水分以外のガスを除く装置を有す
る請求項8に記載のガスの利用装置。9. The gas utilization apparatus according to claim 8, further comprising a device for removing gases other than methane, sulfur compounds, carbon dioxide, and moisture downstream of the dehumidifying mechanism.
を用いるガスの利用方法であって、前記ガス圧縮機によ
り前記圧縮機と前記背圧手段の間の配管及び前記分岐部
分と前記減圧手段の間の分岐配管中のガスの圧力を高
め、次いで前記減圧手段によりこのガスを減圧し、減圧
後のガス圧が前記貯蔵手段における圧力よりも高いガス
を消費設備に供給することを包含するガスの利用方法。10. A method of using gas using the apparatus according to claim 1, wherein the gas compressor is used to connect the pipe between the compressor and the back pressure means, the branch portion, and the pipe. Increasing the pressure of the gas in the branch pipe between the depressurizing means, then depressurizing this gas by the depressurizing means, and supplying to the consuming facility a gas whose depressurized gas pressure is higher than the pressure in the storage means. How to use gas.
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JP2001226036A JP3939509B2 (en) | 2001-07-26 | 2001-07-26 | Method and apparatus for using gas |
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JP2001226036A JP3939509B2 (en) | 2001-07-26 | 2001-07-26 | Method and apparatus for using gas |
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JP3939509B2 JP3939509B2 (en) | 2007-07-04 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7472542B2 (en) | 2003-10-30 | 2009-01-06 | Hitachi, Ltd. | Gas-turbine power generating installation and method of operating the same |
CN109210376A (en) * | 2018-11-02 | 2019-01-15 | 中国石油天然气集团公司 | A kind of gas pipeline hot standby regulator online |
-
2001
- 2001-07-26 JP JP2001226036A patent/JP3939509B2/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7472542B2 (en) | 2003-10-30 | 2009-01-06 | Hitachi, Ltd. | Gas-turbine power generating installation and method of operating the same |
CN109210376A (en) * | 2018-11-02 | 2019-01-15 | 中国石油天然气集团公司 | A kind of gas pipeline hot standby regulator online |
CN109210376B (en) * | 2018-11-02 | 2023-05-16 | 中国石油天然气集团有限公司 | Online hot standby pressure regulating device of gas pipeline |
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JP3939509B2 (en) | 2007-07-04 |
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