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JP2511227B2 - Method for producing power generation fuel and power generation method - Google Patents
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JP2511227B2 - Method for producing power generation fuel and power generation method - Google Patents

Method for producing power generation fuel and power generation method

Info

Publication number
JP2511227B2
JP2511227B2 JP26459892A JP26459892A JP2511227B2 JP 2511227 B2 JP2511227 B2 JP 2511227B2 JP 26459892 A JP26459892 A JP 26459892A JP 26459892 A JP26459892 A JP 26459892A JP 2511227 B2 JP2511227 B2 JP 2511227B2
Authority
JP
Japan
Prior art keywords
power generation
fuel
low
sulfur content
crude oil
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.)
Expired - Lifetime
Application number
JP26459892A
Other languages
Japanese (ja)
Other versions
JPH06207179A (en
Inventor
睦範 唐崎
正樹 飯島
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP26459892A priority Critical patent/JP2511227B2/en
Publication of JPH06207179A publication Critical patent/JPH06207179A/en
Application granted granted Critical
Publication of JP2511227B2 publication Critical patent/JP2511227B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/10Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はコンバインド・サイクル
発電用燃料の製造方法およびその燃料を用いるコンバイ
ンド・サイクル発電方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a fuel for combined cycle power generation and a combined cycle power generation method using the fuel.

【0002】[0002]

【従来の技術】現在日本における火力発電としては、ボ
イラにより生じた高温高圧のスチームでタービンを回転
させて発電するスチームタービンによる方法が主なもの
である。そのボイラ用油燃料としては主に重油や原油が
使用されている。それらの内、原油焚きの場合はワック
ス分が多く、かつSOxの発生量の少ない低硫黄含有原
油、例えばミナス産原油や大慶産原油が好んで使用され
ている。そのほか、最近では良質燃料であるLNGを用
いたコンバインド・サイクル発電法も採用されている。
2. Description of the Related Art At present, as a thermal power generation in Japan, a method using a steam turbine for rotating a turbine with a high-temperature and high-pressure steam generated by a boiler to generate electric power is mainly used. Heavy oil and crude oil are mainly used as the oil fuel for the boiler. Among them, in the case of crude oil burning, low-sulfur content crude oil with a large amount of wax and low SOx generation amount, for example, crude oil from Minas and crude oil from Daqing are preferably used. In addition, recently, a combined cycle power generation method using LNG, which is a good fuel, has been adopted.

【0003】前記原油や重油のボイラ焚きおよびスチー
ムタービンによる発電では熱効率が40%前後/HHV
基準(HHV:高位発熱量)と比較的低い。これに対
し、LNG焚きで採用されているコンバインド・サイク
ル発電では圧縮機で圧縮した空気で燃料を燃焼させる
か、あるいは該圧縮空気を燃焼熱で加熱させ、その高温
高圧ガスでタービンを回転させて発電させ、さらにその
排ガスをボイラで回収し、スチームタービンを運転して
再度発電する方法であり、熱効率が48%前後/HHV
基準と高いことが特徴である。
Thermal efficiency is about 40% / HHV in power generation by the boiler burning of crude oil or heavy oil and steam turbine.
It is relatively low compared to the standard (HHV: Higher heating value). On the other hand, in combined cycle power generation adopted in LNG-fired combustion, fuel is burned by air compressed by a compressor, or the compressed air is heated by combustion heat, and a turbine is rotated by the high-temperature high-pressure gas. This is a method of generating power, collecting the exhaust gas with a boiler, and operating a steam turbine to generate power again. Thermal efficiency is around 48% / HHV.
It is characterized by high standards.

【0004】[0004]

【発明が解決しようとする課題】石油の埋蔵量には限界
があり、石油の消費量増大の抑制の見地から、発電に使
用する石油類の使用が国際的に制限されるようになっ
た。すなわち発電に使用する石油消費量を現状で凍結し
なければならなくなっている。従って発電設備の老朽化
により設備を新設する際には、燃料使用量の増加によら
ないで今後の電力需要増に対処するため、熱効率の高い
発電方法への転換に迫られている。
The reserves of petroleum are limited, and the use of petroleum for power generation has come to be restricted internationally from the viewpoint of suppressing the increase in petroleum consumption. In other words, the amount of oil used for power generation must be frozen at present. Therefore, when new equipment is installed due to deterioration of power generation equipment, it is necessary to switch to a power generation method with high thermal efficiency in order to cope with future power demand increase without increasing fuel consumption.

【0005】また前記LNGによるコンバインド・サイ
クル発電では既に高熱効率による発電が行われている
が、LNGは貯蔵にコストがかかる関係上、原油に比べ
安定供給に不安を残している。欧米では既に原油や残渣
油をガスタービンの燃料に使用している実績があるが、
それらに含まれる不純物のためトラブルが多く発生し、
軽油やLNGを使用する場合に比べ保守費用が嵩む問題
点が指摘されている。ガスタービンに使用する油燃料の
不純物含有量として、塩分を0.5ppm以下、硫黄分
を0.05重量%以下、バナジウムを0.5ppm以下
に制限することが望ましいとされている。特に塩分とバ
ナジウムは相互に影響してガスタービンのブレード金属
の溶融点を低下させたり、灰分のブレードへの粘着の原
因となる。ボイラ焚き燃料として使用されている前記ミ
ナス産原油や大慶産原油のような低硫黄含有原油でも、
これらの基準を満足できず、熱効率のよいコンバインド
・サイクル発電のガスタービン燃料としてそのまま転用
できないという問題がある。
Further, in the combined cycle power generation by LNG, power generation with high thermal efficiency has already been performed, but LNG has a concern about stable supply as compared with crude oil because storage costs high. In Europe and the United States, we already have a record of using crude oil and residual oil as fuel for gas turbines.
A lot of troubles occur due to the impurities contained in them,
It has been pointed out that maintenance costs are higher than when using light oil or LNG. It is said that it is desirable to limit the salt content to 0.5 ppm or less, the sulfur content to 0.05 wt% or less, and the vanadium to 0.5 ppm or less as the impurity content of the oil fuel used for the gas turbine. In particular, salinity and vanadium interact with each other to lower the melting point of the blade metal of the gas turbine and cause ash to stick to the blade. Even low-sulfur content crude oil such as the above-mentioned Minas crude oil or Daqing crude oil used as a boiler burning fuel,
There is a problem that these criteria cannot be satisfied, and they cannot be diverted as they are as gas turbine fuel for combined cycle power generation with good thermal efficiency.

【0006】[0006]

【課題を解決するための手段】本発明者らは低硫黄含有
原油を熱効率のよいコンバインド・サイクル発電の燃料
に使用する方法について鋭意検討した結果、コンバイン
ド・サイクル発電で使用する燃料の内、ガスタービン用
には前記不純物含有量の少ない燃料が必要であるもの
の、ボイラにおいては不純物含有量の制限が比較的緩や
かであること、低硫黄含有原油は一般にワクシーであ
り、バナジウムなどの重金属含有量も少ない傾向にある
こと、さらにこのような低硫黄含有原油を簡単な脱塩処
理と蒸留により低沸点留分と高沸点留分に分離すること
により必要な全ての基準を満たすガスタービン用燃料お
よび排熱ボイラ用燃料が得られることに注目し、本発明
を完成させることができた。
Means for Solving the Problems The inventors of the present invention have made earnest studies on a method of using low-sulfur-containing crude oil as a fuel for combined cycle power generation with high thermal efficiency. As a result, among the fuels used in combined cycle power generation, gas Although a fuel with a low content of impurities is required for turbines, the restrictions on the content of impurities in the boiler are relatively lenient, and low-sulfur content crude oil is generally waxy, and the content of heavy metals such as vanadium is also low. Gas turbine fuels and exhaust gas that meet all the required criteria by separating these low sulfur content crude oils into low boiling fractions and high boiling fractions by simple desalination and distillation. The present invention has been completed, paying attention to the fact that a fuel for a heat boiler can be obtained.

【0007】すなわち本発明の第一の要旨は塩分含有量
を0.5ppm以下に調整した低硫黄含有原油を常圧蒸
留または減圧蒸留により硫黄含有量が0.05重量%以
下の低沸点留分よりなるコンバインド・サイクル発電の
ガスタービン燃料と硫黄含有量が0.05重量%を超え
る高沸点留分よりなるボイラ燃料とに分離することを特
徴とする発電用燃料の製造方法であり、また、本発明の
第二の要旨は塩分含有量を0.5ppm以下に調整した
低硫黄含有原油を常圧蒸留または減圧蒸留により硫黄含
有量が0.05重量%以下の低沸点留分と硫黄含有量が
0.05重量%を超える高沸点留分とに分離し、前記低
沸点留分をコンバインド・サイクル発電のガスタービン
の燃料に用い、前記高沸点留分をボイラの燃料に用いる
ことを特徴とする発電方法である。
That is, the first gist of the present invention is that a low-sulfur content crude oil having a salt content adjusted to 0.5 ppm or less is subjected to atmospheric distillation or vacuum distillation to obtain a low-boiling fraction having a sulfur content of 0.05% by weight or less. A method for producing a fuel for power generation, characterized in that it is separated into a gas turbine fuel for combined cycle power generation and a boiler fuel consisting of a high boiling fraction having a sulfur content of more than 0.05% by weight. The second gist of the present invention is to subject a low-sulfur content crude oil having a salt content adjusted to 0.5 ppm or less to atmospheric distillation or vacuum distillation to obtain a low-boiling fraction having a sulfur content of 0.05% by weight or less and a sulfur content. Is separated into a high boiling point fraction exceeding 0.05% by weight, the low boiling point fraction is used as a gas turbine fuel for combined cycle power generation, and the high boiling point fraction is used as a boiler fuel. Do It is an electrical method.

【0008】[0008]

【実施例】以下、本発明のコンバインド・サイクル発電
用燃料の製造方法およびその燃料を用いるコンバインド
・サイクル発電方法を図1によって説明し、併せて本発
明の作用を明らかにする。図1では主要設備のみ示し付
属設備は省略してある。本発明で用いられる低硫黄含有
原油としては燃焼排ガスの脱硫工程を簡略化できること
からできるだけ硫黄含量の少ないものが好ましいことは
いうまでもないが、通常硫黄含有量が1重量%以下、さ
らに好ましくは0.9重量%以下の原油が用いられる。
このような原油としては前記のワックス分の多いミナス
産原油や大慶産原油などをあげることができる。このよ
うな原油に含まれるバナジウム量は通常0.4〜0.5
ppmである。これらの低硫黄含有原油としてミナス産
原油は硫黄含有量が約0.1重量%以下と少なく特に好
ましい。
EXAMPLE A method for producing a fuel for combined cycle power generation according to the present invention and a method for combined cycle power generation using the fuel will be described below with reference to FIG. 1, and the operation of the present invention will be clarified. In FIG. 1, only main equipment is shown and auxiliary equipment is omitted. Needless to say, as the low-sulfur content crude oil used in the present invention, one having as low a sulfur content as possible is preferable because the desulfurization process of combustion exhaust gas can be simplified, but usually the sulfur content is 1% by weight or less, more preferably Crude oil up to 0.9% by weight is used.
Examples of such crude oil include the crude oil produced in Minas and the crude oil produced in Daqing mentioned above, which are rich in wax. The amount of vanadium contained in such crude oil is usually 0.4 to 0.5.
It is ppm. Minas crude oil is particularly preferable as the low-sulfur content crude oil because it has a sulfur content of about 0.1% by weight or less.

【0009】本発明においては、このような低硫黄含有
原油を脱塩処理工程1により塩分含有量を0.5ppm
以下に調整する。脱塩方法としては通常原油の脱塩処理
に用いられる方法がそのまま適用できる。すなわち、原
油に水を加えて洗浄し水層を分離すれば塩分含有量は低
下する。通常の石油精製では塩分含有量が3ppm以下
としているが、前記水洗脱塩方法を繰り返すことにより
容易に塩分含有量を0.5ppm以下とすることができ
る。
In the present invention, such a low-sulfur content crude oil is subjected to a desalting treatment step 1 so that the salt content is 0.5 ppm.
Adjust as follows. As the desalting method, the method usually used for desalting crude oil can be directly applied. That is, if water is added to the crude oil to wash it and the aqueous layer is separated, the salt content decreases. In ordinary petroleum refining, the salt content is set to 3 ppm or less, but the salt content can be easily set to 0.5 ppm or less by repeating the water washing desalting method.

【0010】塩分含有量を0.5ppm以下に調節した
低硫黄含有原油は常圧蒸留工程2または減圧蒸留工程3
により硫黄含有量が0.05重量%以下の低沸点留分と
硫黄含有量が0.05重量%を超える高沸点留分に分離
される。両蒸留はどちらか一方のみでもよいし、常圧蒸
留で分離された沸点の高い留分をさらに図1に示すよう
に減圧蒸留してもよい。使用原油により硫黄含有量が境
界値0.05重量%を超える沸点留分および留分割合が
異なるが、前記ミナス産原油の場合は軽油留分(常圧沸
点に換算して約340〜460°F以下)ないしガス留
分(同460〜650°F)以下の沸点留分とそれを超
える沸点留分に分離することにより、硫黄含有量0.0
5重量%の低沸点留分が約4割、硫黄含有量が0.05
重量%を超える高沸点留分が約6割の割合で得られる。
しかも該低沸点留分にはバナジウムなどの重金属は殆ど
検出されず、コンバインド・サイクル発電のガスタービ
ン用燃料として適するものである。
The low-sulfur content crude oil having a salt content adjusted to 0.5 ppm or less is subjected to an atmospheric distillation step 2 or a vacuum distillation step 3.
Thus, a low boiling fraction having a sulfur content of 0.05% by weight or less and a high boiling fraction having a sulfur content of more than 0.05% by weight are separated. Either one of the both distillations may be performed, or the fraction having a high boiling point separated by the atmospheric distillation may be further distilled under reduced pressure as shown in FIG. Depending on the crude oil used, the boiling point fraction having a sulfur content exceeding the boundary value of 0.05% by weight and the fraction of the fraction differ, but in the case of the above-mentioned Minas crude oil, a light oil fraction (converted to a normal pressure boiling point of about 340 to 460 ° F or less) to a gas fraction (both 460 to 650 ° F) or less and a boiling point fraction higher than that to obtain a sulfur content of 0.0
Approximately 40% of low boiling point fraction of 5% by weight, sulfur content of 0.05
High-boiling fractions in excess of weight% are obtained in a proportion of about 60%.
Moreover, almost no heavy metal such as vanadium is detected in the low boiling fraction, and it is suitable as a gas turbine fuel for combined cycle power generation.

【0011】前記ミナス産原油の典型例では、脱塩処理
により塩分含有量を0.5ppm以下に調整した原油を
沸点650°F以下の留分とそれを超える留分とに分離
した場合、650°F以下の留分割合は43.2体積%
であり、硫黄含有量は0.033重量%、バナジウムは
検出されないコンバインド・サイクル発電のガスタービ
ン用燃料が得られた。この低沸点留分を採取した後の残
渣油(REDUCED−CRUDE、沸点650°F以
上、比重26.5°API、流動点106°F)は硫黄
含有量が約0.15重量%と良質重油並に低く、ドナジ
ウム/ニッケル/鉄分の各含有量は約1/15/10p
pmであり、ボイラ用燃料としては何ら支障なく使用で
きるものであった。
In a typical example of the above-mentioned crude oil produced by Minas, when crude oil having a salt content adjusted to 0.5 ppm or less by a desalting treatment is separated into a fraction having a boiling point of 650 ° F. Fraction below 4 ° F is 43.2% by volume
The sulfur content was 0.033% by weight, and vanadium was not detected, so that a fuel for gas turbine of combined cycle power generation was obtained. The residual oil (REDUCED-CRUDE, boiling point 650 ° F or higher, specific gravity 26.5 ° API, pour point 106 ° F) after collecting the low boiling fraction has a sulfur content of about 0.15% by weight and is a good quality heavy oil. Medium low, each content of dnadium / nickel / iron is about 1/15 / 10p
It was pm and could be used as a boiler fuel without any trouble.

【0012】本発明において、使用する低硫黄含有原油
により硫黄含有量が0.05重量%を超える高沸点留分
(あるいは残渣油)の割合が多い場合は、これをさらに
分離して前記ガスタービン用基準を満たす燃料を採取す
ることも可能である。このような残渣油を分離する方法
としては、高温・高圧の溶剤を用いる公知の超臨界溶剤
抽出・分離工程4(例えば特開昭57−31989号公
報、特開昭59−170191号公報)を用いることが
できる。
In the present invention, when the proportion of high-boiling fraction (or residual oil) having a sulfur content of more than 0.05% by weight is large depending on the low-sulfur content crude oil to be used, this is further separated to obtain the gas turbine. It is also possible to collect fuel that meets the usage standards. As a method for separating such residual oil, a known supercritical solvent extraction / separation step 4 (for example, JP-A-57-31989, JP-A-59-170191) using a high temperature / high pressure solvent is used. Can be used.

【0013】[0013]

【発明の効果】以上詳細に述べたように、従来の低硫黄
含有原油をボイラ焚きに使用して発電する場合と異な
り、本発明では脱塩処理した低硫黄含有原油から常圧蒸
留または減圧蒸留で低沸点留分と高沸点留分に分離する
ことにより、必要な全ての基準を満たすガスタービン用
燃料およびボイラ用燃料が得られる。これらの燃料をコ
ンバインド・サイクル発電に使用することにより、全量
をボイラで焚いてスチームタービンで発電する場合の熱
効率約40%前後に比べ高熱効率の約48%前後で発電
することができ、省エネルギーおよびCO2 による地球
温暖化防止の観点から極めて有利である。
INDUSTRIAL APPLICABILITY As described in detail above, unlike the conventional case where a low-sulfur content crude oil is used for boiler-fired power generation, in the present invention, a desulfurized low-sulfur content crude oil is subjected to atmospheric distillation or vacuum distillation. By separating the low boiling point fraction and the high boiling point fraction with, a gas turbine fuel and boiler fuel satisfying all the required criteria can be obtained. By using these fuels for combined cycle power generation, it is possible to generate power at about 48% of high thermal efficiency as compared to about 40% of thermal efficiency when the entire amount is burned by a boiler and power is generated by a steam turbine. It is extremely advantageous from the viewpoint of preventing global warming by CO 2 .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明が適用される低硫黄含有原油からコンバ
インド・サイクル発電用燃料を製造するプロセスの説明
図。
FIG. 1 is an explanatory diagram of a process for producing a fuel for combined cycle power generation from crude oil containing low sulfur to which the present invention is applied.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 塩分含有量を0.5ppm以下に調整し
た低硫黄含有原油を常圧蒸留または減圧蒸留により硫黄
含有量が0.05重量%以下の低沸点留分よりなるコン
バインド・サイクル発電のガスタービン燃料と硫黄含有
量が0.05重量%を超える高沸点留分よりなるボイラ
燃料とに分離することを特徴とする発電用燃料の製造方
法。
1. A combined cycle power generation system comprising a low boiling point distillate having a sulfur content of 0.05% by weight or less by atmospheric distillation or vacuum distillation of a low sulfur content crude oil having a salt content adjusted to 0.5 ppm or less. A method for producing a fuel for power generation, which comprises separating a gas turbine fuel and a boiler fuel composed of a high boiling fraction having a sulfur content of more than 0.05% by weight.
【請求項2】 塩分含有量を0.5ppm以下に調整し
た低硫黄含有原油を常圧蒸留または減圧蒸留により硫黄
含有量が0.05重量%以下の低沸点留分と硫黄含有量
が0.05重量%を超える高沸点留分とに分離し、前記
低沸点留分をコンバインド・サイクル発電のガスタービ
ンの燃料に用い、前記高沸点留分をボイラの燃料に用い
て発電することを特徴とする発電方法。
2. A low-sulfur-containing crude oil having a salt content adjusted to 0.5 ppm or less is subjected to atmospheric distillation or vacuum distillation to a low-boiling fraction having a sulfur content of 0.05% by weight or less and a sulfur content of 0. A high boiling point fraction exceeding 05% by weight is separated, and the low boiling point fraction is used as a fuel for a gas turbine for combined cycle power generation, and the high boiling point fraction is used as a fuel for a boiler to generate electricity. How to generate electricity.
JP26459892A 1992-10-02 1992-10-02 Method for producing power generation fuel and power generation method Expired - Lifetime JP2511227B2 (en)

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JP2511227B2 true JP2511227B2 (en) 1996-06-26

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5057315B2 (en) * 1998-10-30 2012-10-24 日揮株式会社 Method for producing gas turbine fuel oil
JP2001073715A (en) * 1999-09-08 2001-03-21 Mitsubishi Heavy Ind Ltd High-efficiency power generation system
JP4509267B2 (en) * 1999-11-15 2010-07-21 日揮株式会社 Oil fuel-fired combined power generation facility and method thereof

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