TWI277655B - Fuel gas moisture monitoring apparatus and method of monitoring fuel gas moisture - Google Patents

Fuel gas moisture monitoring apparatus and method of monitoring fuel gas moisture Download PDF

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Publication number
TWI277655B
TWI277655B TW094137125A TW94137125A TWI277655B TW I277655 B TWI277655 B TW I277655B TW 094137125 A TW094137125 A TW 094137125A TW 94137125 A TW94137125 A TW 94137125A TW I277655 B TWI277655 B TW I277655B
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Taiwan
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gas
temperature
fuel gas
pressure
fuel
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TW094137125A
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Chinese (zh)
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TW200716765A (en
Inventor
Masaaki Sako
Yujiro Fujisaki
Masahiko Koketsu
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Kawasaki Plant Systems Kk
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/22Fuels, explosives
    • G01N33/225Gaseous fuels, e.g. natural gas
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N19/00Investigating materials by mechanical methods
    • G01N19/10Measuring moisture content, e.g. by measuring change in length of hygroscopic filament; Hygrometers
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/22Fuels, explosives

Abstract

Fuel gas moisture monitoring apparatus (1) that has a simple and robust construction and exhibits stable monitoring capability. The fuel gas moisture monitoring apparatus (1) includes gas extraction piping (14) for sampling of an aliquot of fuel gas having been fed to fuel gas supply facilities; fuel gas thermometer (15) disposed at a region of fuel gas supply piping (5) where the fuel gas is set for the state of steam saturation; squeezing member (16) for reducing of the pressure of gas having been sampled by the gas extraction piping (14) to substantially the same pressure as the steam saturation pressure at the temperature detected by the fuel gas thermometer (15); sample gas cooler (13) for adjusting of the temperature of the sample gas having been brought to substantially the same pressure as the steam saturation pressure to the temperature in the vicinity of the temperature detected by the fuel gas thermometer (15); and drain pot (18) fitted with a drain detector for detecting of any water condensed from the sample gas.

Description

1277655 九、發明說明: 【發明所屬之技術領域】 法。關於燃料氣之濕分監測裝置及濕分監測方 .有之濕分:裝置:::監測供應至燃燒設備之燃料氣所含 ~ 【先前技術】 於製鐵業中,例如,舍 J戈 田以呵爐法生產生鐵時,合您古 爐產生作為掉生痛轉^ 勹件生乳體之爐頂氣體(Blast Furnace > 稱為「BFG」)。近车杳装认… s以下 ^ 、 近年末基於郎約能源等目的,以此等拉 生氣體作為燃氣輪機發電設備 又1用心燃科*1的例子日益增多。 又’亦逐漸開發出一猶古、,、、土令 種问爐法之外的新製鐵製程(例如, ™與⑺贿法等之直接還原鐵法),將此等新製 產生之伴生氣體作為„來有效制㈣子亦日漸增多。 面此等拌生氣體中,除了含有硫化氫、氰 氫、氯化合物、硫化幾、氨等雜質外,亦含有水基氣。又, :般而言,由於拌生氣體在產生時為高溫而藉由水之喷霧 寺來冷卻’因此在作為嫩祖$卡 、 社邗馮燃枓虱來供應時,其中 飽和狀態。 …矾馮 將上述氣體作為燃料使用情 # ν卜,晏乳體中之濕分 因某些原因而超過既定上限傯宏 ^ , 疋上限饭疋值日r,會在燃料氣供應 ^ … 此^是結水會附著於燃料氣供應 ό又備、燃k设備、排熱回收設備| 又°又備寻之配官或機器類,而有 可能因與上述雜質之相互作用而產生相。又,燃料氣中 之濕分右大幅增加’作為燃料之發熱量即相對降低,而亦 6 1277655 有可月b導致使用此燃料氣之燃燒設備的 機單機或發電設備整體之效率降低。 L孔輪 、拌生氣體為燃料之燃氣輪機發電設備中,由 於拌生氣體之供應屬力為低遷(大氣塵+數i mmAq左 須用㈣機對其進行厂堅、縮。當被塵縮之拌生氣體 :4狀悲時’濕分會凝結而產生水滴’而有可能於壓 產生腐姓或塵埃附著導致麼縮效率降低。如此,使燃 :氣保持乾燥狀態’係為了防止機器腐敍、確保I缩機性 =維持發電設備效率之前提條件。然而,燃料氣之掉生 y為自然產生之氣體’係—氣體特性不斷變動的氣體, 因此無法由此氣體的產生源直接控制。 =除去燃料氣中之濕分’已有一種具備用以麼縮姆 ”孔機構、冷卻機構、水分吸附機構的燃料氣供應裝 知、專利文獻1 )。 " 之不2:為了進行燃料氣之有效除濕或偵測與濕分相關 料氣中原因,雖較佳者係進行濕分監測來確認出燃 分為飽和以下的狀態,但以往並未進行例如燃 二:之燃料氣中的濕分監測,因此並無監測技術。例如, 二::::一射式、靜電容式、電阻式等… 為一般之軋體中的濕分檢測器以監測燃料氣中 但由於此等主要係用以檢測大氣中之濕分” 氣二::並不適用於對具有毒性、可燃性、腐㈣之掉: 二二行具可靠性的監測。為了檢測出異常情形,用 "里燃料氣濕分之測量器,須係-可長期間持續穩定; 7 -1277655 揮性能之可靠性高的裝置。 專利文獻1 :日本特開2004— 92565號公報 【發明内容】 本&月為解決上述課題,其目的在於提供渴 軍u 、货、 ^ ,、μ w 促伏濕分監測仏 置測方法,其在檢測拌生氣體等之_氣中的渴1277655 IX. Description of the invention: [Technical field to which the invention pertains] Law. About the moisture monitoring device for the fuel gas and the moisture monitoring device. There are moisture points: Device::: Monitor the fuel gas supplied to the combustion equipment. [Prior Art] In the iron industry, for example, She J. When the iron is produced by the method, the furnace gas (Blast Furnace > called "BFG") is produced as a raw milk for the birth of the baby. In the near-car 认 认 ^ ^ ^ 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于 基于In addition, it has gradually developed a new ironmaking process (such as TM and (7) brittle method and other direct iron reduction methods) in addition to the method of the order of the ancient order, such as the associated gas produced by the new system. As the „effective system (4) is also increasing, the mixing gas contains water-based gas in addition to impurities such as hydrogen sulfide, hydrogen cyanide, chlorine compounds, sulfurized, ammonia, etc. Because the mixed gas is high in temperature and is cooled by the spray of water, it is saturated when it is supplied as a tender card, and it is saturated. Fuel use situation # ν Bu, the wetness of the 晏 emulsion exceeds the established upper limit for some reasons 偬 macro ^, 疋 upper limit rice cooker value r, will be in the fuel gas supply ^ ... This is the water will adhere to the fuel Gas supply and preparation, burning equipment, heat recovery equipment | and ° looking for the official or machine type, and may be due to the interaction with the above impurities to produce phase. In addition, the moisture in the fuel gas The right increase is 'relatively lower as the calorific value of the fuel, but also 6 12 77655 There is a possibility that the efficiency of the machine or the power generation equipment of the combustion equipment using this fuel gas is reduced. The L-hole wheel and the mixed gas are fuel gas turbine power generation equipment, because the supply of the mixed gas is low. (Atmospheric dust + number i mmAq left must be used for (4) machine to make it firm and shrink. When mixed with dust and dust: 4 sorrows, 'wet points will condense and produce water droplets' and may cause pressure to produce rot or Dust adhesion leads to a reduction in the efficiency of the shrinkage. Thus, keeping the combustion gas in a dry state is a condition to prevent the machine from being rotted and to ensure the reduction of the efficiency of the power generation equipment. However, the fuel gas is naturally generated. The gas 'system' is a gas whose gas characteristics are constantly changing, so it cannot be directly controlled by the source of the gas. = The moisture content in the fuel gas is removed, and there is a hole mechanism, a cooling mechanism, and moisture adsorption. The fuel gas supply and installation of the organization, patent document 1). " No. 2: In order to effectively dehumidify the fuel gas or detect the moisture-related gas, it is preferred to perform moisture monitoring to confirm that the fuel is below saturation, but it has not been carried out in the past. For example, the second part of the fuel gas monitoring in the fuel gas, so there is no monitoring technology. For example, two:::: one-shot, static-capacitance, resistive, etc... is a wet-spot detector in a general rolling body to monitor fuel gas but because these are mainly used to detect moisture in the atmosphere." Gas 2:: Not suitable for the toxicity, flammability, and rot (4): The reliability of the 22nd line is monitored. In order to detect the abnormal situation, the measuring instrument for the fuel gas moisture is required. It is a device that can be stably stabilized for a long period of time; 7 -1277655 is a device having high reliability. Patent Document 1: Japanese Laid-Open Patent Publication No. 2004-92565. SUMMARY OF THE INVENTION This is to solve the above problems. , goods, ^,, μ w volts and moisture monitoring sputum test method, its thirst in the detection of mixed gas

::二Γ用特殊的裝置,可依據單純原理,藉由將現 二〃有使用績效之機器或測量器作為其要素來加以 ,、且口’即可使可靠性提高且增長使用壽命。 應4發然料氣之濕分監測裝置,係設置於燃料氣供 〜又”寸欲在於,具有:氣體抽取褒置,係對供庫至 燃料氣供㈣之㈣—輕咖樣;職應至 -的心::襞置,係用以使以該氣體抽取裝置取樣之氣 :二=與供應至燃料氣供應設備之燃料氣的水蒸氣 釦和/1力大致相同的壓力, ^ 5 ^ ^ I便4樣扣虱體之溫度成為供 二主Ht礼钣應設備之燃料氣 —# ώ y ii LL ” 瘵氣飽和溫度附近的溫 度精此私測由該樣品氣體產生之凝結水。 =此種構成,#所供應之燃料氣中之濕分 可得知燃料氣中濕分之增加產生之凝結水。藉此,即 當該燃料氣供應設備具備养 之加埶梦罟々、人"、” "’夜肢熱媒來加熱燃料氣 取狀置、…2 Η叙置的至少-裝置時,該氣體抽 從該加熱裝置或冷卻裂置之下游側進行燃料 二==要係、用水等液體熱媒來進行燃料氣之加熱或冷 -斷換器’罐漏出至燃 性 8 -1277655 零。因此,若從此等裝置之下游側的樣品氣體檢測出凝結 水的話,即可推測燃料氣中之濕分增加的原因為上述裝 置。 該濕分檢測裝置’具備· ^ 氣體溫度檢測器,係設置於燃料氣供應設備中燃料氣 ^ 被設定為水蒸氣飽和狀態的燃料氣通路; 氣體壓力調節裝置,係用以使以該氣體抽取裝置取樣 " 之氣體壓力,成為與該氣體溫度檢測器之檢測溫度的水蒸 • 氣飽和壓力大致相同的壓力; 氣體溫度調節裝置,係用以使與水蒸氣飽和壓力大致 相同之壓力的該取樣氣體溫度,成為該氣體溫度檢測器之 檢測溫度附近的溫度;以及 凝結水偵測器,係檢測來自該樣品氣體之凝結水。 ' 又,亦能構成為,該氣體壓力調節裝置,係將樣品氣 • 體之壓力設定為水蒸氣飽和壓力; 該氣體溫度調節裝置,係將樣品氣體溫度設定為較該 ® 氣體溫度檢測器之檢測溫度高既定值的溫度; 該凝結水偵測器,係可檢測是否有從樣品氣體產生凝 • 結水。 ; 如此,藉由將樣品氣體溫度設定為較水蒸氣飽和溫度 _ 高既定值,而能在燃料氣中之濕分比例在通常之無問題範 圍内變動、或產生測量誤差時,吸收此等來維持穩定監測 動作。而且在實際偵測到凝結水之產生時,即可判斷燃料 氣中之濕分已增加。 9 -1277655 又,亦能構成為,該氣體壓力調節裝置,係將樣品氣 月旦之塵力设疋為水療氣飽和壓力; ^ 該氣體溫度調節裝置,係將樣品氣體溫度設定為較嗜 氣體溫度檢測器之檢測溫度低既定值的溫度; 該凝結水偵測器,係可檢測出從樣品氣體產生之 水的產生量。 如此,藉由將樣品氣體溫度設定為較水蒸氣飽和溫度 低既定值,即使燃料氣為水蒸氣飽和狀態而產生凝結2 = 但稭由凝結水檢測器所檢測之凝結水產生量即可判斷燃 氣中之濕分是否有增加。 …y 該氣體壓力調節裝置,亦可係由形成於燃料氣之取樣 通路的節流構件構成。 7 :可設有複數組成對之該氣體溫度調節褒置與凝結水 H ’各氣體溫度調節裝置,係將被該氣體壓力調節穿 ^周整為4壓力之樣品氣體調整為互異的溫度。藉此方义 声’即使例如燃料氣中之濕分增加時,由於可對應增加程 二::數組之對來依序㈣凝結水,因此可得知濕分比例 ^ . τ;、另廣刀監測裝置,係设於燃料氣供應設備, 供應設備具備以液體熱媒加熱流通於燃料供應通 …枓乳的加熱裝置、&用以冷卻之冷 -者’其特徵在於,具備: 中的至’ 冷卻=循環通路,係使液體熱媒循環於所有加熱裝置或 10 1277655 及 熱媒貯留容器,係將熱媒供應至該熱媒循環通路; 以 熱媒檢測裝置,係檢測該熱媒貯留容器内之_^ 依據該熱媒檢測裝置之檢測結果,來偵側埶媒里’ 從加熱裝置或冷卻褒置茂漏至燃料氣供應通路内。、有 依據此構成,例士 g #、 要, 如即使發生在該加熱裝置或冷卻缺 =料氣中混人液體熱媒導致燃料氣中之濕分增加的^ 由於此%即《熱媒貯留容器往熱媒循環ϋ路補充執 二因此藉由檢測出熱媒貯留容器内之熱媒 充: 可察覺上述事態。 亿即 本务明之燃料氣之濕分監測方法,係監測 應至燃燒設備之氣體的濕分,其特徵在於,包含.供 氣體抽取步驟’係對所供應之燃料氣-部分進行取樣; 壓力溫度調節步驟,係使所取樣 所供應之烬料氣的士从a 土刀成马與 "、、科乳的水条氣飽和遷力大致相同的壓力,並成 為所f應之燃料氣的水蒸氣飽和溫度附近的溫度;以及 凝結水檢測步驟,你 糸彳欢測成為上述壓力及溫度之樣品 氣to所產生之凝結水; 依據該凝結水檢測結果來監測燃料氣之濕分。 該壓力溫度調整步驟,包含·· 氣體溫度檢測步驟’係檢測設定為水蒸氣飽 燃料氣的溫度; 氣體壓力調節步|平 & 土 q 係使该氣體抽取步驟中取樣之氣 月豆的壓力,成為與該氣體溫度檢測步驟中所檢測之溫度的 11 "1277655 水蒸氣飽和壓力為大致相同的壓力;以及 氣體溫度調節步驟,係使該氣體抽取步驟中取樣之氣 體的溫度,成為與該氣體溫度檢測步驟中所檢測之溫度附 近的溫度。 又,於該氣體壓力調節步驟中,使樣品氣體壓力成為 水蒸氣飽和壓力; ^於該氣體溫度調節步驟中,使樣品氣體溫度成為較該 氣體溫度檢測步驟中之檢測溫度高既定值的溫度·, t於該凝結水檢測步驟中,檢測是否有從樣品氣體產生 藉此來監測濕分。 使樣品氣體壓力成為 又,於該氣體壓力調節步驟中 水蒸氣飽和壓力; 〜於該氣體溫度調節步驟中’使樣品氣體溫度成為較該 礼體溫度檢測步驟中之檢測溫度低既定值的溫度; 人 測出來自樣品氣體之;疑結:: The special device can be used according to the simple principle, by using the existing machine or measuring device with performance as its element, and the reliability can be improved and the service life can be increased. The moisture monitoring device should be set up in the fuel gas supply. It is set in the fuel gas supply. It has: gas extraction device, and is supplied to the fuel gas supply (4) (4) - light coffee sample; To the heart:: the device is used to make the gas sampled by the gas extraction device: 2 = the same pressure as the water vapor button and /1 force of the fuel gas supplied to the fuel gas supply device, ^ 5 ^ ^ I will 4 the temperature of the carcass to become the fuel gas for the two main Ht ceremony equipment - # ώ y ii LL 温度 The temperature near the saturation temperature of the helium gas is measured by the condensate produced by the sample gas. = such a composition, the moisture content in the fuel gas supplied by # can be known as the condensed water generated by the increase in the moisture content in the fuel gas. In this way, when the fuel gas supply device has at least a device for raising the fuel gas, such as at least the device, which is used to heat the fuel gas. The gas is pumped from the downstream side of the heating device or the cooling crack to perform fuel heating, or a liquid-heating medium such as water for heating the fuel gas or the cold-disconnector's tank to the flammability 8-1277655. Therefore, when the condensed water is detected from the sample gas on the downstream side of the apparatus, it is estimated that the cause of the increase in the moisture content in the fuel gas is the above-mentioned apparatus. The moisture fraction detecting apparatus 'provides · ^ gas temperature detector, is set In the fuel gas supply device, the fuel gas is set to a fuel gas passage in a state of water vapor saturation; the gas pressure adjusting device is configured to cause the gas pressure of the gas sampling device to be "the gas pressure detector" The temperature at which the water is vaporized and the gas saturation pressure are substantially the same; the gas temperature adjusting device is used to make the temperature of the sample gas at a pressure substantially equal to the saturation pressure of the water vapor as the gas The temperature detector detects the temperature near the temperature; and the condensate detector detects the condensed water from the sample gas. 'Also, the gas pressure adjusting device can set the pressure of the sample gas and body. The water vapor saturation pressure; the gas temperature adjustment device sets the sample gas temperature to a temperature higher than a predetermined temperature of the ® gas temperature detector; the condensate detector detects whether there is a sample gas Condensation • Condensation. ; Thus, by setting the sample gas temperature to a higher than the water vapor saturation temperature _ high, the ratio of moisture in the fuel gas can be varied within the usual problem-free range, or measurement error can occur. At this time, absorb this to maintain a stable monitoring action, and when the actual generation of condensed water is detected, it can be judged that the moisture content in the fuel gas has increased. 9 -1277655 Further, the gas pressure adjusting device can also be configured The dust of the sample gas is set to the spa gas saturation pressure; ^ The gas temperature adjustment device sets the sample gas temperature to be more gassing. The body temperature detector detects a temperature at which the temperature is lower than a predetermined value; the condensate detector detects the amount of water generated from the sample gas. Thus, by setting the sample gas temperature to be lower than the water vapor saturation temperature The established value, even if the fuel gas is saturated with water vapor, produces condensation 2 = but the amount of condensed water detected by the condensate detector can determine whether the moisture in the gas increases. ...y The gas pressure regulator It may also be constituted by a throttle member formed in the sampling passage of the fuel gas. 7 : The gas temperature regulating device and the condensed water H' may be provided with a plurality of pairs of gas temperature adjusting devices, which are to be pressurized by the gas The sample gas which is adjusted to the pressure of 4 cycles is adjusted to a mutually different temperature. By means of this sound, even if, for example, the moisture content in the fuel gas increases, the condensed water can be sequentially (4) due to the addition of the second:: array pair. Therefore, it can be known that the moisture content ratio is τ; and the other wide-knife monitoring device is provided in the fuel gas supply device, and the supply device is provided with the liquid heat medium heated to flow through the fuel supply... The heating device, & cooling for cooling, is characterized in that: the middle to the 'cooling=circulation path, the liquid heat medium is circulated to all the heating devices or 10 1277655 and the heat medium storage container, which is hot The medium is supplied to the heat medium circulation passage; the heat medium detecting device detects the detection result of the heat medium detecting device according to the detection result of the heat medium detecting device, and detects the side of the medium from the heating device or the cooling device Leak into the fuel gas supply path. According to this configuration, the case g #, want, if even in the heating device or cooling shortage = the gas mixed with the liquid heat medium causes the moisture in the fuel gas to increase ^ because of this %, "heat medium storage The container is replenished to the heat medium circulation circuit so that the above-mentioned state of affairs can be detected by detecting the heat medium charge in the heat medium storage container. The method of monitoring the moisture content of the fuel gas of the present invention is to monitor the moisture content of the gas to be supplied to the combustion equipment, characterized in that it comprises: the gas extraction step 'sampling the supplied fuel gas portion; the pressure temperature The adjustment step is to make the sampled supply of the sputum gas from the a knives into a horse and the pressure of the water saturation of the water, and become the fuel gas of the fuel gas. The temperature near the vapor saturation temperature; and the condensate detection step, you are decimating the condensed water produced by the sample gas to the above pressure and temperature; and monitoring the moisture content of the fuel gas based on the condensed water detection result. The pressure temperature adjustment step includes: · the gas temperature detecting step 'detects the temperature set to the steam saturated fuel gas; the gas pressure adjusting step | the flat & the soil q system causes the gas of the gas sample to be sampled in the gas extraction step And the pressure is substantially the same as the temperature of 11 "1277655 water vapor saturation pressure detected in the gas temperature detecting step; and the gas temperature adjusting step is such that the temperature of the gas sampled in the gas extraction step becomes The temperature near the temperature detected in the gas temperature detecting step. Further, in the gas pressure adjusting step, the sample gas pressure is made to be a water vapor saturation pressure; and in the gas temperature adjusting step, the sample gas temperature is set to a temperature higher than a predetermined temperature in the gas temperature detecting step. In the condensed water detecting step, it is detected whether or not there is a sample gas generated thereby to monitor the moisture content. And causing the sample gas pressure to be again, in the gas pressure adjusting step, the water vapor saturation pressure; in the gas temperature adjusting step, 'the sample gas temperature is a temperature lower than a predetermined temperature in the body temperature detecting step; The person measured the gas from the sample;

於該凝結水檢測步驟中,檢 水量; 藉此來監測濕分。 仅據本發明,藉由採用單純之原理及 可裎也叮土 间平心稱成,即 -可罪性高且使用壽命長的濕分監測裝置。且壯 維修保養頻度與校正頻度亦較低。 衣之 【實施方式】 =照圖式說明本發明之燃料氣濕分監測裝置及濕分故 去之-實施形態。圖】為燃氣輪機發電設備4 : 1夕不 12 1277655 其具有設有本發明-實施形態之燃料氣濕分監測 濕分監二燃料氧供應設備,2、以及燃氣輪機3。本發明之 備4。、置之適用對象亚不特別限定於此燃氣輪發電設 源=中’例如在高爐或直接還原鐵設備等之氣體產生 i的拌生氣體,係作為燃氣輪機3用之姆料供岸 至燃料氣供應設備2的氣體供庫配 广、應 撼, “配g 5中。在到達燃氣輪 之氣體供應配管5途中’從其上游側依序設有電氣集 ::二氣體加熱器乂:低壓燃料氣&縮機(以下簡稱為低 二1 :侣”8、中間冷部器9、以及高壓燃料氣壓縮機(以下 間稱為高壓壓縮機)1G。如此,此燃料氣供應設備2,係以 =壓及高壓之二段來壓縮燃料氣,在二段壓縮步驟間藉由 間冷郃器9來進行燃料氣之冷卻。當然,本發明之適用 對象並非限定於上述構成之設備。 方;此氣體供應配管5連技古门、、去吃t ^ g J逑接另回流官1 1,其能使燃氣輪 之入口前至低壓壓縮機8之上游側間之燃料氣的至少 一部分回流。例如,當送電系統產生異常而須瞬間壓縮(使 其減少)燃料氣之供應量時,由於當塵縮機7, 8之氣體流量 車乂 /柃即T產生浪湧現象(surging),而有可能導致振動產 生,因此可藉此回流管11來避免此情況。回流管11下游 端之與氣體供應配管5的連接位置,只要係在對此燃料氣 供應設備2供應燃料氣之位置到低壓壓縮機8為止之低壓 管線的話’任一位置皆可。於此回流f 11’從其上游側依 序設有止流閥〗2與氣體冷卻器13。一般而言,此回流管 13 •1277655 】係方、燃氣輪機3起動時使用,在 止流閥12,佶上,γ ^ 運鈐¥即闕閉上述 前述氣妒Λ办 建乳體冷卻器13盥 引这孔紅加熱器7及中間冷卻器9, - 之溫水或;人7^梦、—A 馬糟由流通於管内 器。當然,介74 P M科我的熱交換 、亦可使用其他種類之加熱器盥冷呷哭 —部=濕分監測裝置b係從氣體供應二:對燃料氣 刀仃取樣,並檢測此樣品氣體中之、、 拗料氣谁;Τ π此 販τ之濕分。用以對此In the condensed water detecting step, the amount of water is checked; thereby, the moisture score is monitored. According to the present invention, a wet-separation monitoring device having a high sinfulness and a long service life is known by using a simple principle and a flattening between the earth and the earth. And the maintenance frequency and correction frequency are also low. [Embodiment] The fuel gas moisture monitoring device and the wet separation method of the present invention are described in the following description. Fig. 1 is a gas turbine power generation facility 4: 1 eve 12 12277655 which has a fuel gas moisture monitoring wet separation monitoring fuel oxygen supply device, 2, and a gas turbine 3 provided with the present invention. Preparation 4 of the present invention. The applicable object is not particularly limited to the gas turbine power generation source=zhong', for example, a gas generated by a gas such as a blast furnace or a direct reduction iron device, which is used as a gas for the gas turbine 3 to supply the fuel to the fuel. The gas supply device 2 is equipped with a wide range of gas supply and storage, "with g 5 in the middle. On the way to the gas supply pipe 5 of the gas wheel", an electric set is provided from the upstream side thereof: two gas heaters: A low-pressure fuel gas & refrigerating machine (hereinafter referred to as a low-grade 1: a middle) 8, an intermediate cold unit 9, and a high-pressure fuel gas compressor (hereinafter referred to as a high-pressure compressor) 1G. Thus, the fuel gas supply device 2 The fuel gas is compressed by the second stage of the pressure and the high pressure, and the fuel gas is cooled by the intercooling unit 9 during the two-stage compression step. Of course, the object to which the present invention is applied is not limited to the apparatus having the above configuration. Fang; this gas supply pipe 5 is connected to the ancient gate, and to eat t ^ g J逑 and another returning official 1 1, which can make at least the fuel gas between the inlet of the gas turbine and the upstream side of the low pressure compressor 8 Part of the reflow. For example, when the power transmission system generates an abnormality, it must be instantaneous. When the supply amount of the fuel gas is reduced (to reduce), the gas flow turbulence/柃, that is, the T of the dust reduction machine 7, 8 causes a surge, which may cause vibration, so that it can be recirculated. The tube 11 is used to avoid this. The connection position of the downstream end of the return pipe 11 to the gas supply pipe 5 is as long as it is at the low pressure line to the low pressure compressor 8 at the position where the fuel gas supply device 2 supplies the fuel gas. In this case, the return flow f 11' is sequentially provided with a check valve 2 and a gas cooler 13 from the upstream side thereof. Generally, the return pipe 13 • 1277655 is used when the gas turbine 3 is started, Stop valve 12, 佶上, γ ^ 钤 阙 阙 阙 阙 阙 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 上述 这 这 这 这 这 这 这 这^Dream, - A horse is circulated in the tube. Of course, I can exchange heat with other types of heaters, and can also use other types of heaters to chill and cry - part = wetness monitoring device b is from gas supply two: Sampling the fuel gas knives and detecting the contents of the sample gas Who is the gas; Τ π this is the wetness of the τ

管5之中;^人氣體抽取配f 14’係連接於氣體供應配 “部器9與高級缩機間的部分(圖中以符 :表不)。如後所述,此氣體抽取配管14之下 連接於氣體供應配管5 ’、 4立如 心电孔木麈益6與回流管U的連Among the tubes 5, the human gas extraction and the f 14' are connected to the gas supply portion "the portion between the portion 9 and the high-level reduction machine (in the figure, the symbol: not shown). As will be described later, the gas extraction pipe 14 Connected to the gas supply piping 5 ', 4, such as the heart of the electric hole Muyuyi 6 and the return pipe U

接邛之間(圖中以符號D 供應配管5。 以使樣口口亂體回流到氣體 料氣供應設備2中’為了進行燃料氣之冷卻係以 :賀霧’而以水蒸氣飽和狀態供應至氣體供應配管5。又, 於電氣集塵器6中再藉由以水噴霧來除去塵埃。電氣集塵 器6,係藉由水霧分離器來除去燃料氣中之液體成分。婉 如此處理之燃料氣在到達氣體加熱器7之前,可想見大致 係水蒸氣飽和狀態。又’ 一般而t,在藉由氣體加熱器7 加‘4後亚在到達燃氣輪機3之前,燃料氣係保持於水蒸氣 飽和未滿之狀態(乾燥狀態)。 然而,當萬一電氣集塵器6之水霧分離器未將燃料氣 之液體成分充分地除去、或液體熱媒從氣體加熱器7或中 間冷卻器9漏出至燃料氣中之事態產生時,燃料氣即會變 14 -1277655 化為水蒸氣飽和或過飽和的狀態。其結果,即有可能於燃 料氣供應設備2之低溫部位附著凝結水。因此,濕分監測 裝置1,係設置於有可能會因某些原因導致燃料氣成為水 蒸氣飽和以上之狀態的部分。亦即,本實施形態中,係設 置於電氣集塵器6到燃氣輪機3間之氣體供應配管5。 ”、、"见π取1 i,对所坟直邵位之燃Between the joints (the pipe is supplied with the symbol D in the figure D. In order to allow the sample port to flow back into the gas material supply device 2, the water gas is saturated with water for the cooling of the fuel gas. To the gas supply pipe 5. Further, the dust is removed by spraying with water in the electric dust collector 6. The electric dust collector 6 removes the liquid component in the fuel gas by a mist separator. Before the fuel gas reaches the gas heater 7, it is conceivable to be substantially saturated with water vapor. Again, in general, after the gas heater 7 is added '4, the fuel gas system remains before the gas turbine 3 is reached. The state in which the water vapor is not saturated (dry state). However, if the water mist separator of the electric dust collector 6 does not sufficiently remove the liquid component of the fuel gas, or the liquid heat medium is cooled from the gas heater 7 or the intermediate When the event of the leakage of the device 9 into the fuel gas is generated, the fuel gas is changed to a state in which the water vapor is saturated or supersaturated by 14 to 1277655. As a result, it is possible to adhere the condensed water to the low temperature portion of the fuel gas supply device 2. , The sub-monitoring device 1 is provided in a portion where the fuel gas may be saturated with water vapor for some reason. That is, in the present embodiment, the gas is disposed between the electric dust collector 6 and the gas turbine 3 Supply piping 5. ",, " see π take 1 i, the burning of the grave

料氣樣品進行減壓減溫。亦即,藉由使樣品氣體之壓力溫 度Ρ牛低至與燃料氣取樣位置上游側之水蒸氣飽和狀態的辦 料氣大致相同的壓力溫度,來㈣凝結水(以下亦稱為排水 (d·))。藉此方式來監測燃料氣之濕分。上述水蒸氣飽和 狀態之燃料氣壓力及溫度係可稱為「基準壓力」及「美準 溫度」。此基準溫度係_ 1中氣體供應配管5上之_ I4氣溫度言十15之部位的燃料氣溫度。由於此部位之燃料 孔在正*狀恶下係保持為水蒸氣飽和狀態,因此基準壓力 即為該基準溫度之水蒸氣飽和壓力。 方;上述氣體抽取配管1 41 μ ^ γ t + ^ 攸其上游側起依序設有節流 構件16,係作為用以降低揭σ > t . _ 低樣°〇軋體壓力之氣體壓力調節裝 置,樣口口氣體冷卻器丨7, ^ ^ _ ,、乍為用以々部樣品氣體之氣體 胍度凋即发置;以及排水 水容哭1 s . σσ ,係用以收集排水。此排 [:8,可發揮檢測出樣品氣體嶋氣)之渴分的凝社 “功能。於排水容器設有用以檢測是否有產生排: 之排水檢測器(未圖示)。排水檢測器:水 的檢測器。例如,採用蕤 用Α知且適用 „ 由因產生排水之電氣導诵决、佳― 偵測者、偵測排水之重量 ' V、末進订 者、偵測排水之貯水水位者等。 15 *1277655 虱體抽取配官14之下游側,如前所述,係連接於氣體 仏應配官5之電氣集塵器、6與回流f i i之連接部間的位 置氣體抽取配管14下游側之此連接部位d,係一流經 ^處氣體供應配管5之燃料氣通常為保持於水蒸氣飽和狀 〜的位置。X ’為了使其不受經由回流管i】而回流之高 壓燃料氣的影響而連接於⑽f η之連接部的上游側。 據此’上述節流構件16下游側之氣體抽取配管14内 的軋體壓力’係和流經氣體供應配管5之與氣體抽取 配官14下游側連接之部位D的燃料氣壓力(上述基準壓力) Μ °又’樣品氣體之溫度’係藉由樣品氣體冷卻器17, 冷部至較流經氣體供應配管5之與氣體抽取配I Μ下游 側連接之部位D的燃料氣溫度(為上述基準溫度,圖2中 以符號Ts顯示)略高的溫度(目標溫度)。 圖2係顯示從氣體產生源s供應之燃料氣經由 塵器6、氣體加熱器7、低壓壓” 而& 甲間冷部态9,從 取樣點C通過氣體抽取管14,再經由樣品氣體冷卻哭17 ^非水容器18而到達與氣體供應配管5之連接點D為止, ,、溫度變化之一例。圖2之縱軸表示 — 礼肢溫度,橋為目丨丨本 示氣體通過之上述機器類等。 八' 如圖1所示,於樣品氣體冷卻器1 ^ WW V 下私側設有樣品氣 月且/皿度汁19。又,於樣品氣體冷卻器 管? 1 Μ古Η丨v , Μ 1 7之冷部水供應配 :夕:又有…郎冷卻水流量之流量調整間η。 叫氣體冷卻态I 7來作為用以將樣品氣體 7 的溫度調節裝置,直理由在於様σ …即冲目標溫度 ”理由在方'樣〇口軋體為較基準溫度Ts 16 ^77655 度Ta之故。上述燃料氣溫度計15、節流構件μ、 體冷卻器17、排水容器18及樣品氣體溫度計", 、可稱為用以檢測燃料氣之濕分的濕分檢測褽置。 樣。,品=體冷卻器17’係藉由控制裝置2〇之控制來使 ::乳體溫度成為上述目標溫度。亦即,控制裝置20,係 声”述基準溫度Ts高些許之溫度(Ts+ △”作為目標溫 二错由調節上述冷卻水供應配管21之流量調整閥η的 二/消除以樣品氣體溫度計19檢測出之樣品氣體實 不:皿又Ta與目標溫度Ts+ △ t的偏差。為了檢測出燃料氣 刀s加〇超過水療氣飽和點者),而將樣 為基準溫度及基準麼力時,基於下述理由,須使用以檢測 排水之樣品氣體的目標溫度成為較基準溫度(飽和溫幻& 高些許。亦即,由於會因燃料氣之特性微小變動、或辦料 f路之狀態會受其設置場所之環境條件的變化影響而導致 誤差產生,因此其係用以吸收此等誤差。 此目標溫度與基準溫度之差At’由於可決定成對應基 氣表(蒼照圖3)所示之既定水蒸氣分屢(換言之,為燃料氣 中水分之體積比例),因此可根據燃料氣溫度來變更。亦即, △ t會隨設定成水蒸氣飽和之上述低壓線中之燃料氣溫度 而改變。如圖3所示,燃料氣之水蒸氣㈣的變化比例(水 蒸氣分壓對燃料氣温度變化之變化)’係在燃料氣溫度越高 時即越大。如此,由於係將設定成對應既定水基氣分 壓,因此所供應之燃料氣溫度較高時之^即低於所供應 之燃料氣溫度較低時之“的溫度差。例如,如圖3所示, 17 -1277655 雖對應燃料氣溫度為20〜30°C附近時水分之體積比例為約 2%(圖3中以符號Μ表示)的溫度差為約i〇°c (圖3中以符 唬N表不)’但對應燃料氣溫度為60°C附近時水分之體積 比例為約2%(圖3巾以符號X表示)的溫度差為約2t (圖3 少 表不)。圖3中,縱軸係取水蒸氣分壓、橫軸 係取燃料氣溫度(水蒸氣溫度)來顯示飽和水蒸氣線。 如此,即使以水蒸氣飽和狀態供應之燃料氣藉由氣體 加:°。7等而成為過熱蒸氣狀態,藉由使此燃料氣回復到 原來之接近水療氣飽和的壓力溫度來檢測有無排水,即可 偵測出燃料氣中濕分是否異常增加。例如,圖1所示之實 施形態中,能檢測出因電氣集塵器6、氣體加熱器7及; 間冷部器9中之水分、、曰Α 增 刀此入而導致之濕分的增加。為此目的, 孔月“:應配g 5中之燃料氣之取樣位置(亦即氣體抽取配管 連接位置C)只要係在中間冷卻器9下游、且在燃氣 輪機3上游之任奄仂番 …… , ^ P可。又,萬一於氣體抽取配管14 之樣品氣體冷卻器1 7中古日 有/”、、刀入到燃料氣中時,由於 在其下游設有排水容器1 8 6因此亦可加以檢測。 圖4係顯示另_揪粗* 乂抖乳供應設備23。此設備23中, 係於氣體供應配管5僅钟古 L ^ σ又有^又燃料壓縮機5 0。且亦未設 置中間冷卻器9。又,盥中η σ ,、中間冷部益9同樣地,上述氣體 加熱荔7亦亚非本發明 心义要構成構件。此燃料氣供應設 備23中,濕分監測裝置 凡 仏5又置於燃料氣壓縮機50下游 侧。由於此濕分監測裝f 置之構成與圖1之濕分監測裝置 1在貫貝上為相同的構成,因此 ^ ’略洋細說明。藉由此濕 18 *1277655 分監測農1卜例如在電氣集塵器6及氣體力… = 入燃料氣中而導致滿分增加時,可加以-為此目的,氣體供應配管5之燃料氣之取樣位置(亦 管14之連接位置)只要係在氣體加熱器7下游4 在燃氣輪機3上游之任意位置即可。 如上述說明’濕分監測裝置i之設置位置、 供應配管5與氣體抽取配管14之連接位置C,若,心 料氣中有可能混入濕分之機器下 " 好季乂為便利。亦即,如圖 所不"刀別於圖!之燃氣輪機發電設備”鹿 广低壓壓縮機8及中間冷卻器9之下游側設置… 測t置24、1。如此,藉由以特/、、孤 分,即可大致在任一機器6、7、8:檢測出濕 疋否已爲人濕分。因此,可採取適#且迅速的處置。 …圖5,係對與圖i相同之配管及相同之機器賦予相同 m略其詳細說明。於電氣集塵器' 縮機…間冷卻器9之間、以及緊鄰中間冷卻器= :側^別連接有氣體抽取配管14。在低㈣縮機8與中間 ’二°P :。9間及中間冷卻器9下游側的濕分監測裝置1在實 v上為相同構成,兩濕分監測裝i 1之氣體抽取配管& :仁互相連接,且其τ游端連接於氣體供應配ι $中和電The gas sample is depressurized and desuperheated. That is, (4) condensed water (hereinafter also referred to as drainage (d·), by making the pressure of the sample gas yak as low as the pressure of the water vapor saturated state of the upstream side of the fuel gas sampling position. )). In this way, the moisture content of the fuel gas is monitored. The fuel gas pressure and temperature in the above-mentioned water vapor saturation state can be referred to as "reference pressure" and "US standard temperature". This reference temperature is the fuel gas temperature at the portion of the gas supply pipe 5 at the temperature of the gas supply pipe 5. Since the fuel hole in this portion is maintained in a water vapor saturation state under the positive stagnation, the reference pressure is the water vapor saturation pressure of the reference temperature. The gas extraction pipe 1 41 μ ^ γ t + ^ 攸 is provided with a throttle member 16 in the upstream side thereof as a gas pressure for reducing the pressure of the rolling body pressure The adjusting device, the sample mouth gas cooler 丨7, ^ ^ _ , and 乍 are the gas enthalpy of the gas used for the sputum sample; and the drainage water is crying for 1 s. σσ is used to collect drainage. This row [:8, which can play the role of detecting the sample gas helium) is a function of the thirsty. The drainage container is provided with a drainage detector (not shown) for detecting whether or not there is a discharge row. Drainage detector: Water detectors, for example, use Α 且 且 且 适用 由 由 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气 电气And so on. 15 *1277655 The downstream side of the body extraction and dispensing unit 14 is connected to the downstream side of the position gas extraction pipe 14 between the electric dust collector of the gas chamber 5 and the connection portion between the gas and the reflow fii. The connection portion d is a fuel gas of the first-class gas supply pipe 5, which is usually maintained at a position where the water vapor is saturated. X ′ is connected to the upstream side of the connection portion of (10) f η in order not to be affected by the high-pressure fuel gas that flows back through the return pipe i]. According to this, the "rolling body pressure in the gas extraction pipe 14 on the downstream side of the throttle member 16" and the fuel gas pressure flowing through the portion D of the gas supply pipe 5 connected to the downstream side of the gas extraction company 14 (the above-mentioned reference pressure) Μ ° and 'the temperature of the sample gas' is the temperature of the fuel gas from the sample gas cooler 17 to the portion D of the gas supply pipe 5 connected to the downstream side of the gas extraction port I (the above reference) The temperature, shown by the symbol Ts in Fig. 2) is a slightly higher temperature (target temperature). 2 shows that the fuel gas supplied from the gas generation source s passes through the dust collector 6, the gas heater 7, the low pressure pressure, and the cold junction state 9, passes from the sampling point C through the gas extraction pipe 14, and then passes through the sample gas. An example of temperature change is obtained by cooling the crying 17 ^ non-aqueous container 18 and reaching the connection point D with the gas supply pipe 5. The vertical axis of Fig. 2 indicates the temperature of the ritual limb, and the bridge is the above-mentioned gas passage. Machine class, etc. 八' As shown in Figure 1, the sample gas cooler 1 ^ WW V is placed on the private side of the sample gas month and / dish juice 19. Also, in the sample gas cooler tube? 1 Μ古Η丨v , Μ 1 7 cold water supply: 夕: There is ... Lang cooling water flow rate adjustment between η. Gas cooling state I 7 as a temperature adjustment device for the sample gas 7, the reason is 様σ ... is the target temperature. The reason is that the square-like rolling stock is at a reference temperature Ts 16 ^ 77655 degrees Ta. The fuel gas thermometer 15, the throttle member μ, the body cooler 17, the drain container 18, and the sample gas thermometer may be referred to as wet moisture detecting means for detecting the moisture content of the fuel gas. kind. The product = body cooler 17' is controlled by the control device 2 to make the ::milk temperature the target temperature. That is, the control device 20 detects that the reference temperature Ts is a little higher (Ts + Δ) as the target temperature, and the second/elimination of the flow rate adjustment valve η of the cooling water supply pipe 21 is detected by the sample gas thermometer 19 The sample gas is not: the deviation of the vessel Ta from the target temperature Ts+ Δt. In order to detect that the fuel gas knife s is more than the spa gas saturation point, and the sample is the reference temperature and the reference force, based on For the reason, the target temperature of the sample gas to be used for detecting the drainage is higher than the reference temperature (saturation temperature & a little higher. That is, because the characteristics of the fuel gas may change slightly, or the state of the material f will be affected by it. The error is caused by the change of the environmental conditions of the installation place, so it is used to absorb the error. The difference between the target temperature and the reference temperature At' can be determined as the corresponding base gas meter (as shown in Figure 3). The predetermined water vapor is repeatedly (in other words, the volume ratio of moisture in the fuel gas), so it can be changed according to the temperature of the fuel gas. That is, Δt is in the low-voltage line which is set to be saturated with water vapor. The temperature of the feed gas changes. As shown in Fig. 3, the change ratio of the water vapor (four) of the fuel gas (the change of the partial pressure of water vapor to the change of the temperature of the fuel gas) is larger as the temperature of the fuel gas is higher. It will be set to correspond to the predetermined water-based gas partial pressure, so the temperature of the supplied fuel gas is higher than the temperature difference when the supplied fuel gas temperature is lower. For example, as shown in Figure 3, 17 -1277655 The temperature difference of the volume ratio of water when the fuel gas temperature is around 20 to 30 ° C is about 2% (indicated by the symbol Μ in Fig. 3) is about i〇 °c (in Figure 3, the symbol N) It is shown that 'but the temperature difference of the water volume when the fuel gas temperature is around 60 ° C is about 2% (the symbol of Figure 3 is indicated by the symbol X) is about 2t (Fig. 3 is less). In Fig. 3, The vertical axis is the partial pressure of water vapor, and the horizontal axis is the temperature of the fuel gas (water vapor temperature) to indicate the saturated water vapor line. Thus, even if the fuel gas supplied in the state of water vapor saturation is added by gas: °, etc. Superheated vapor state, by returning this fuel gas to its original pressure close to the spa gas saturation The temperature is used to detect the presence or absence of drainage, and it is possible to detect whether the moisture content in the fuel gas is abnormally increased. For example, in the embodiment shown in Fig. 1, the electric dust collector 6, the gas heater 7, and the intercooling portion can be detected. The moisture in the device 9 and the increase in the moisture content caused by the addition of the knife. For this purpose, the hole month ": should be equipped with the sampling position of the fuel gas in g 5 (that is, the gas extraction pipe connection position C) As long as it is downstream of the intercooler 9 and upstream of the gas turbine 3, ^ P. In addition, in the sample gas cooler of the gas extraction pipe 14 in the ancient day, there is /", the knife When it is introduced into the fuel gas, it can also be detected by providing a drain container 186 downstream thereof. Fig. 4 shows another 揪 揪 乂 乂 milk supply device 23. In this device 23, the gas supply pipe 5 is only the clock L ^ σ and the fuel compressor 50. Also, an intercooler 9 is not provided. Further, in the same manner as in the middle of the η σ and the intermediate cold portion, the gas heating 荔 7 is not a component of the present invention. In the fuel gas supply device 23, the moisture monitoring device is placed on the downstream side of the fuel gas compressor 50. Since the configuration of the wetness monitoring device is the same as that of the wetness monitoring device 1 of Fig. 1, it is described in detail. By monitoring the agricultural product, for example, in the wet dust collector 6 and the gas force... = into the fuel gas, for example, when the full-scale increase is caused, the fuel gas sampling of the gas supply pipe 5 can be taken for this purpose. The position (also the connection position of the tube 14) may be any position downstream of the gas heater 3 at the downstream of the gas heater 7. As described above, the installation position of the wetness monitoring device i and the connection position C between the supply pipe 5 and the gas extraction pipe 14 may be facilitated by mixing the moisture in the heart gas. That is, as shown in the figure, the knife is different from the figure! The gas turbine power generation equipment" is set on the downstream side of the Luguang low-pressure compressor 8 and the intercooler 9. The measurement t is set to 24, 1. Thus, by means of special /, orphan, it can be roughly in any machine 6, 7, 8: It is detected that the wetness is already wet. Therefore, it can be taken as a quick and timely treatment. Fig. 5 is a detailed description of the same piping and the same machine as that of Fig. i. The dust collector's between the reducer and the intercooler 9 and the intercooler = : the side is connected to the gas extraction pipe 14. In the low (four) reducer 8 and the middle 'two ° P: 9 and intermediate cooling The wetness monitoring device 1 on the downstream side of the device 9 has the same configuration on the real v, and the gas extraction pipes of the two wetness monitoring devices i1 are connected to each other, and the τ swimming end is connected to the gas supply and the neutralization. Electricity

氣集塵器6與回;;奋營! ! +h A 口抓& 11之連接部間的位置D。兩濕分監 ,置1,樣品氣體均藉由節流構件16而成為前述基準壓力, 二由樣品氣體冷卻器17控制成較基準溫度Ts稍高的溫度 由於取樣位置不同’因此兩節流構件16係設 19 1277655 疋成不同的流路阻抗值。 此外,在低壓壓縮機8與中間冷卻器9間連接監測用 虱體抽取配管14之理由在於,因從電氣集塵器6至低壓 壓縮機8之流路阻抗較小,使緊臨氣體加熱器7之下游位 置的燃料氣壓力、與氣體抽取配管丨4下游端之燃料氣壓 •力的差過小,而導致樣品氣體無法充分流通之故。基於此 理由,而將壓力較高之低壓壓縮機8下游側作為取樣位置。 # 另一方面,設置於電氣集塵器6上游之濕分監測裝置 24係與上述濕分監測裝置i不同,並未在其氣體抽取配管 14設置節流構件與樣品氣體冷卻器,而設有用以確保取樣 流量之定量I 51及排水容器18。χ,此氣體抽取配管14 係與4述兩濕分監測裝置丨之氣體抽取配管1 4連接而合 -流。未設置節流構件及樣品氣體冷卻器之理由在於,樣品 氣體之取出係在電氣集塵器6與氣體加熱器7之間、亦即 為水蒸氣飽和狀態之燃料氣流通之處。因此,樣品氣體不 _ 、、咸I亦不須冷卻。只須於水蒸氣飽和狀態下直接進行燃 =氣之取樣來檢測其有無排水即可。當然,為了使樣品氣 版μ度成為較基準溫度Ts稍高的溫度(Ts + △ t),亦可於 氣抽取配官14之排水容器上游側設置加熱器。 +尸上述說明之實施形態中,雖將以水喷霧至燃料氣中之 =氣集塵器6、使用液體熱媒之氣體加熱器7及中間冷卻 ^ 視為主要的濕分供應源,而於其等之下游側設置濕分 “ ^ =置24、1,但並非限定於此構成。並不限於燃氣輪 機I甩,又備之燃燒設備,即使於其他燃燒設備中,上述機 20 1277655 器類 6、7、Q ^ 、 # 、 Μ外之濕分混入燃料氣中之可能性不為愛 處,均可於1下游伽执菩々 勺v之 、曰、 、下游側5又置濕分監測裝置1。又,亦可於久 漁分監測裝w执署胡丨、,、s J方、各 ^ 置。又置用以通知濕分產生異常之顯示或聲立& 错由女此作法,即可推測在任-機器中是否已 :刀此人燃料氣中,並進行該機器等之修復工程或改善 員的準備’於最適當之時機停止設備之作業,短時 間内進行維修或改善。 τ 圖6 ’係顯示在與氣體供岸配營 配吕5之相冋樣品氣體取 /、備有樣品氣體冷卻@ 17之設定溫度不同的複數 i 測裝置1者。gj 6之燃料氣供應設備2由於係與 圖1所示之設備2相同,因此對與圖1相同之配管及相同 之機器賦予相同符號而省略詳細說明。圖6中,複數組(於 本實施形態中為3組)濕分監測裝置!雖係並列設置,但亦 可係串列設置。不過,從不{百收rt / ik 攸不須將樣品氣體之壓力損失調節 成相同這點來看’以並聯配置為佳。於氣體供應配管5之 樣品氣體取樣位置(中間冷卻器9與高壓壓縮機1〇之間)連 接有-支氣體抽取配管14,此氣體抽取配管㈣分歧成 三支氣體抽取配管14a,14b, I4e。 於上述-支氣體抽取配管14之部分設有節流構件i6。 於分歧之三支氣體抽取配管I4a 14h 171八 %,14b,14c分別設有樣品氣 體冷卻器na,m,i7c、樣品氣體溫度計19a, i9b,…及 排水容器18a,18b, 18c。又,氣體抽取配管14&,丨朴,^乜 再度匯合至-支氣體抽取配f 14,且其下游端連接於氣體 供應配管5之電氣集塵器6與回流管η之連接部間的位 21 1277655 置d。 樣品氣體冷卻器17a, 17b,17c,例如係第一樣品氣體 冷卻器27a之設定溫度為較基準溫度TS稍高的溫度(Ts + △ ti)’第二樣品氣體冷卻器17b之設定溫度為較第一樣品 氣體冷卻器之設定溫度稍高的溫度(Ts+ ,第三 松口口 $ 郃益!7c之設定溫度為較第二樣品氣體冷卻器 之設定溫度稍高的溫度(Ts+ Δη + 。此等之溫 度差甚微小。如此,燃料氣以相同壓力流入各分歧配管14a 14b,⑷,並以微小溫度差流入各排水容器]8a,18b, 18c。, ,分別較樣品氣體冷卻器之設定溫度之基準溫度稍高的 =度Λη’At2,At3’係與前述相同地可決定成對應蒸氣 3)所示之記定水蒸氣分壓(換言之為燃料氣中水 刀的扭積比例)。據此’根據所供應之燃料氣的溫度、亦即 對應設定成蒸氣飽和狀態之上述低壓管線中的溫度來使^ tl,Δΐ2,改變。 而二::構成之濕分監測裝置,在欲檢測出因某些原因 而增加之燃料氣中的濕分 以繁一 Μ … 係有下述二種情形,亦即僅 以弟排水谷器18a檢測排水之第一種情 第二排水容器i 8a〗本u 僮乂弟及 ,此末檢測之第二種情形; 排水容器18a 18b 1心办k 乂及以所有 ^ 5 , 8來榀測之第三種情形。可由图1所 示之蒸氣表預先管屮斜_ 圖3所 將直m广, 容許超過濕分量的溫度差, 為對應第三種情形(例如必須發出警報之情形)之 △ tl + t2 + △ t3。接著,再依序設定對主: 如,必須發出第— 弟一種t形(例 出弟m,警報之情形)之△料心,與 22 1277655 設定對應於第一種情形(例如,必須發出第一階段注意警報 之情形)之△ tl。藉此,即可預告濕分之增加。 作為濕分監測裝置,可取代圖丨,圖4及圖5之濕八 監測裝置1中設置於排水容器18的排水檢測器(亦即僅檢 測排水之有無的排水檢測器),而採用測量每一單位時間之 排水產生量(以下亦稱為流量)的排水測量器。雖未圖示, 此濕分監測裝置之整體構成係與圖丨、圖4及圖5之濕分Gas dust collector 6 and back;; Fen Ying! ! +h A port captures the position D between the <11 connection. The two wet traps are set to 1, the sample gas is the reference pressure by the throttle member 16, and the sample gas cooler 17 is controlled to have a temperature slightly higher than the reference temperature Ts due to the different sampling positions. The 16 series sets 19 1277655 into different flow path impedance values. Further, the reason why the monitoring body extraction pipe 14 is connected between the low pressure compressor 8 and the intercooler 9 is that the flow path resistance from the electric dust collector 6 to the low pressure compressor 8 is small, so that the gas heater is close to The difference between the fuel gas pressure at the downstream position of 7 and the fuel pressure and force at the downstream end of the gas extraction pipe 丨4 is too small, and the sample gas cannot be sufficiently circulated. For this reason, the downstream side of the low pressure compressor 8 having a higher pressure is taken as the sampling position. On the other hand, the moisture monitoring device 24 disposed upstream of the electric dust collector 6 is different from the moisture monitoring device i described above, and is not provided with a throttle member and a sample gas cooler in the gas extraction pipe 14. To ensure the quantitative I 51 of the sampling flow and the drain container 18. Then, the gas extraction pipe 14 is connected to the gas extraction pipe 14 of the two wetness monitoring devices, and is combined. The reason why the throttle member and the sample gas cooler are not provided is that the sample gas is taken out between the electric dust collector 6 and the gas heater 7, that is, the fuel gas flow in the state of water vapor saturation. Therefore, the sample gas is not _, and salt I does not need to be cooled. It is only necessary to directly sample the fuel gas in the state of water vapor saturation to detect the presence or absence of drainage. Of course, in order to make the sample gas plate μ degree slightly higher than the reference temperature Ts (Ts + Δt), a heater may be provided on the upstream side of the drain container of the gas extraction dispenser 14. In the embodiment described above, the gas dust collector 6 using the water spray to the fuel gas, the gas heater 7 using the liquid heat medium, and the intermediate cooling are regarded as the main moisture supply sources. The wet side "^ = 24, 1 is provided on the downstream side of the same, but is not limited to this configuration. It is not limited to the gas turbine I, and the combustion equipment is provided, even in other combustion equipment, the above-mentioned machine 20 1277655 6, 7 , Q ^ , # , Μ 之 之 之 混 混 混 混 混 混 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性 可能性Device 1. In addition, it can also be used in the long-term fishing monitoring equipment, such as Hu Wei,, s J, and each. It is also used to notify the wet spots to produce abnormal displays or sounds. It can be inferred whether or not the machine has been in the machine---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------- τ Figure 6 ' shows the sample gas in the phase with the gas supply camp The sample gas is cooled by a plurality of measuring devices 1 having different set temperatures. The fuel gas supply device 2 of gj 6 is the same as the device 2 shown in Fig. 1, and therefore the same piping and the same machine as those of Fig. 1 are given. The same reference numerals are omitted, and the detailed description is omitted. In Fig. 6, the multiple arrays (three sets in the present embodiment) of the wetness monitoring devices are arranged in parallel, but may be arranged in series. However, never Ik 攸 It is not necessary to adjust the pressure loss of the sample gas to be the same. 'The parallel configuration is preferred. The sample gas sampling position of the gas supply pipe 5 (between the intercooler 9 and the high pressure compressor 1〇) is connected. a gas extraction pipe 14 which is divided into three gas extraction pipes 14a, 14b, and I4e. A throttle member i6 is provided in a portion of the above-mentioned gas extraction pipe 14. The three gas extraction pipes are branched. I4a 14h 171 8%, 14b, 14c are respectively provided with sample gas coolers na, m, i7c, sample gas thermometers 19a, i9b, ... and drain containers 18a, 18b, 18c. Further, gas extraction pipes 14 & ^乜Reunion again a gas extraction device f14, and a downstream end of which is connected to the gas supply pipe 5, and a position 21 1277655 between the connection portion of the electric dust collector 6 and the return pipe η is set. Sample gas coolers 17a, 17b, 17c, for example The set temperature of the first sample gas cooler 27a is a temperature slightly higher than the reference temperature TS (Ts + Δ ti)' The set temperature of the second sample gas cooler 17b is set to be higher than the set temperature of the first sample gas cooler A slightly higher temperature (Ts+, third loose mouth $ 郃 benefits! 7c set temperature is slightly higher than the set temperature of the second sample gas cooler (Ts + Δη + . The temperature difference between these is very small. In this manner, the fuel gas flows into the branch pipes 14a to 14b, (4) at the same pressure, and flows into the respective drain containers 8a, 18b, and 18c with a slight temperature difference. , respectively, slightly higher than the reference temperature of the set temperature of the sample gas cooler = Λ η 'At2, At3' can be determined in the same manner as described above to correspond to the vapor pressure partial pressure shown in the vapor 3) (in other words, fuel) The twist ratio of the water knife in the gas). Accordingly, ?tl, Δΐ2 is changed depending on the temperature of the supplied fuel gas, that is, the temperature in the above-mentioned low-pressure line set to the vapor saturation state. And the second:: the wet-spot monitoring device is configured to detect the moisture in the fuel gas that is increased for some reason to be complicated... The following two situations are used, that is, only the young drainer 18a The first type of drainage water is used to detect the second type of drainage container i 8a〗 This is the second case of the detection of the child, and the second case of the detection; the drainage container 18a 18b 1 the heart and the other 5, 8 to speculate The third case. It can be pre-piped by the steam meter shown in Fig. 1 _ Fig. 3 is wide and wide, and the temperature difference exceeding the wet component is allowed to be Δ tl + t2 + △ corresponding to the third case (for example, when an alarm must be issued) T3. Then, set the pair to the master in order: For example, the Δ center of the t-shaped (the case of the younger brother m, the alarm) must be issued, and the setting of 22 1277655 corresponds to the first case (for example, the first must be issued) At the first stage, pay attention to the situation of the alarm) Δ tl. By this, the increase in moisture content can be predicted. As a wetness monitoring device, instead of the figure, the drain detector provided in the drain container 18 in the wet eight monitoring device 1 of FIGS. 4 and 5 (that is, a drain detector that detects only the presence or absence of drainage) is used for measurement. A drainage gauge for the amount of drainage produced per unit time (hereinafter also referred to as flow rate). Although not shown, the overall composition of the moisture monitoring device is the wetness of the figure, FIG. 4 and FIG.

監測裝置1相同。不同點為如上述般設於排水容器18 ”、I 檢測器係採用測量每一單位時間之排水產生量的測量器, 以及將樣品氣體冷卻器17之設定溫度設定為較基準溫度°丁8 稍低的溫度(Ts— 5 t)。 又 如此,即使係無假定外之濕分增加之健全狀態的燐非 氣’亦將樣品氣體冷卻器17之溫度設定成從其樣品氣骨 會有若干流量之排水產生。此設定溫度與基準溫度之差t t’係與前述Μ同樣地可決定成對應蒸氣表(參照圖3)所3 之既疋水瘵虱分壓。據此’此5 t即根據所供應之煥料^ H亦即根㈣定成水蒸氣飽和狀態之上述低壓管線;| 的燃料氣溫度來改變。 很據此濕分監測裝置,只要因某些原因而使燃料氣 之濕分增加的話’排水產生量即會隨之增加。然後,控 裝置20’例如即會算出從該樣品氣體產生之排水之質量 ,樣品氣體之質量流量的比,據以判斷燃料氣中濕 :加之私度。亦即’由圖3所示之蒸氣表藉由計算預先 出排水之質量流量相對飽和蒸氣狀態之樣品氣體之質量 23 •1277655 量的比,將此比值、與實測 體之質量流量的比進行對比 值較既定值大時即發出警報 之排水之曾备、、六θ丄 貝里/爪$相對樣 ,藉此來判斷。例如,當 品氣 此比 此發出警示之條件以算式表示係如下 (Wa/Ga)/(Ws/Gs)> 1+ α 此處’Ga為實測之樣品氣體的質量流量,^為 樣品產生之排水的實測質量流量’ Ws為算 心:The monitoring device 1 is identical. The difference is that it is provided in the drain container 18" as described above, and the I detector is a measuring device that measures the amount of drainage generated per unit time, and sets the set temperature of the sample gas cooler 17 to be lower than the reference temperature. Low temperature (Ts - 5 t). Again, the temperature of the sample gas cooler 17 is set to have a certain flow from the sample gas bone even if it is not assumed to have a healthy state of increase in wetness. The difference between the set temperature and the reference temperature t t' is determined in the same manner as the above-described enthalpy, and the partial pressure of the water enthalpy of the corresponding vapor table (see Fig. 3) is determined. According to the supply of the material H, that is, the root (4) is determined to be the water vapor saturation state of the above-mentioned low-pressure pipeline; | The fuel gas temperature is changed. According to the moisture monitoring device, as long as the fuel gas is wet for some reason If the amount is increased, the amount of drainage generated will increase. Then, the control device 20' will calculate the mass of the drainage produced from the sample gas, and the ratio of the mass flow of the sample gas, to determine the wetness of the fuel gas: Private. That is The ratio of the ratio of the mass flow rate of the pre-drainage to the mass of the sample gas of the saturated vapor state is 23,1,277,655, and the ratio of the ratio to the mass flow rate of the measured body is compared with the predetermined value. When the value is large, the discharge of the alarm is issued, and the six θ 丄 丄 / 爪 爪 爪 爪 爪 、 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 )/(Ws/Gs)> 1+ α where 'Ga is the mass flow rate of the measured sample gas, and ^ is the measured mass flow rate of the drainage produced by the sample' Ws is the calculation:

和狀態之樣品氣體的質量流量,為從該樣品氣體產= 排水的計算質量流量,α為預估之裕度(贿㈣。上述I 及Gs,係由氣體供應配管5中設定成水蒸氣飽和狀能之電 _器6下游側的溫度及壓力依據圖3所示之蒸 鼻出。 作為流量之測定方法一例,可採用所謂之水位控制。 例如,藉由控制裝置20連續控制排水容器18底部之排出 閥25的開度,使排水容器18之水位維持為—定,從此排 ^閥25之開度算出排水流量。或者,斷續地開關排水容 =18底部之排出閥25來使排水容器18之水位維持為_ 定,再從此開閥週期算出排水流量。#亦可制其他任何 適用之測定方法。 另一方面,樣品氣體之流量可由設置於氣體抽取配管 ^之孔口(orifice)之節流構件16前後的壓力差來算出。此 守 叙可使用既有之設於燃氣輪機發電設備4之燃料氣 供應設備的壓力計26, 27。此壓力計如圖i所示,通常係 設置於低壓壓縮機8入口側之塵力計26及設置於高壓壓 24 1277655 縮機10入口側之壓力計27。兩壓力計26、27雖與節清構 件16相離,但由於從一壓力計27至節流構件丨6入口間 之壓力損失、及從節流構件16之出口至另一壓力計26間 之壓力損失’與緊臨節流構件1 6之前後的差壓相較均相 當小,因此將此等壓力計之測量值視為緊臨節流構件Μ 之如後的壓力來什异氣體流量係無妨礙。如此,可利用既 有之機器來監測燃料氣中之濕分。當然,亦可於緊臨節流 構件16前後之位置分別設置計算氣體流量的壓力計,或 亦可使用液體壓力計(raanoraeter)。 又,測量排水流量,即能根據此測量結果之流量值算 出當時之燃料氣中的水蒸氣分壓。其結果,亦可根據圖3 所示之蒸氣表,判斷當時之燃料氣中的水蒸氣在當初設定 成飽和狀態之氣體供應配管5内的條件下,實際上是否為 飽和蒸氣、或是何種程度之濕蒸氣。 圖7所不者係與圖}所示之燃氣輪機發電設備*相同 的設備,⑥此燃氣輪機發電設備4設有與圖i之濕分監測 衣置1 $同的濕为k測裝置3 i。此濕分監測裝i η,係 專對々部哀置與加熱裝置混入至燃料氣中之濕分進行檢 i的衣置itt吋之冷邠裝置或加熱裝置係使用液體熱媒之 裝置,因此上述渴分臣6、、目丨壯 …、鐵,則放置3 1可說是用以檢測熱媒漏 出至燃料氣中之裝置。 在設於圖7所示之儉少丨尸 < Μ枓氣供應設備2的氣體加熱器7、 中間冷卻器9及氣體冷卻器13,供應至該等之液體熱媒係 循%表其t亦即’如圖所示,所有裝置7、93之熱 25 罾 1277655 制®己管32整體係構成為封閉之迴路。該用以使熱媒猶 環之配管(以下稱為熱媒循環配管)32係連㈣以對其補充 熱媒之熱媒槽33。於熱媒槽33連接有用以將熱媒^槽的 熱媒,應配管34,於此熱媒供應配管34設有止流閱^可 係流量調整閥)35。於熱媒槽33安裝有液面彳%。控㈣ 置20,係根據液面計36之測量結果來開關熱媒供應工配管 W的止流閥35,以控制熱媒槽33内之液面位置 熱媒之量控制成保持於-定。據此,不限定於液面計 可採用可檢測熱媒槽33内之熱媒量的其他公知測量器。 可採用水來作為熱媒。符號37所示者為用以使: 循環配管32的熱縣。符號38所示者為^使 循辰之熱媒冷卻的熱媒用冷卻器。 本實施形態中,熱媒除了被熱媒用冷卻器%冷今以 外三亦供應至中間冷卻器9及氣體冷卻器13來對 心丁冷部。其後’雖供應至氣體冷卻^ i 熱媒泵37而循環,但供應至中間冷卻 :’主 ♦过丄 丨卯9之熱媒則於該 地曰燃料氣而被加熱,且被送至氣體加熱器 側之燃料氣進行加熱。如此,埶蛘 游 不因漏出等而損失, ^致一疋里循環於上述冷卻器與加熱器等。此種情 y …、媒槽33之液面位置不會變動。 冷卻=熱器7、中間冷卻11 9及氣體 埶婵样33…敎漏出至燃料氣中的事態時,由於從 内、之某”3會補充熱媒至熱媒循環配管32,因此熱媒槽A 内之液面會暫時降低。接收來自液面計36之液面降低訊 26 1277655 號後,控制梦 媒循環配管L βρ會開啟止流間35來將熱媒補充至熱 發出邀郝 。又,控制裝置2〇亦依據液面降低訊號而 p oe A L 成之/#、、、刀孤測裒置3 1,亦可杳知渴分 匕此入燃料翕φ沾7从 一·、、、刀 /、 $可此性。或者,亦可根攄用η膝财、老 充至熱媒循環IT根據用以將熱媒補 己吕32中之止流閥35之每一單 閥頻度與開間時間來發出逛彳…母早位_的開 取代止流閥時 …’虽使用流量調整閥來 值大日…、 可义測此閥開度之變化,當開度較既定 值大%即發出警報。 圖8係顯示另一、晶分 測1置。圖8表示者係與圖1 之Μ乳輪機發電設備4相 讯 要〆 扪嗌电δ又備4。此濕分監測裝 置’係利用通常設置於既古 置於既有之發電設備4的測量器類, 此監測由該測定結果算出之 、曰 ,.虱為祛3的發電端效率,根 據其變化來判斷燃料氣中濕分之變化。 圖8係更詳細地顯示錄氧於 ^ 、、、礼輪枝3。此燃氣輪機發電設 觜4〒,雖燃氣輪機3、高壓_ & · 土&%機1 〇、低壓壓縮機8、 以及發電機42係連結於同軸,加# a J釉但並非限定於此構成。壓 縮機8、10亦可遠離燃氣輪機3來配置,而藉由另外之驅 動源來驅動。圖中係顯示燃氣輪 ^ l祝钱3所具備之空氣壓縮機 43及燃燒器44。 上述濕分監測裝置,通常伤刹田〇人 ^ 吊係利用設於既有發電設備4 之氣體供應配管5上的前述燃料氧㈤ 了虱/皿度计1 5、用以測量燃 料氣發熱量(燃燒熱量)之熱量計仏 m , θ … 里寸45、用以測量燃料氣流量 之流量計46、以及設於發電機49 +* 土人, % % 42之發電輸出計47。上述 熱量計45係測量已除去濕分之壯能Α 刀 < 狀恶的(亦即乾燥狀態)燃料 27 !277655 乳發熱量。另—方面, 泠旦。揪斗4灰、田ώ L里δ十46係測量含有濕分之 机里。燃枓軋溫度計15設於 埶旦呌Μ κ 包軋木塵1§ 6之出口附近, 4里计45可設置於氣體供應配 係設於燃燒器44之入口附近之任—位置。流置計46 應配管5内之可能性 Ρ°又於濕分混入氣體供 一 个马;的機器下游側。 藉由使用既有的燃料氣溫度 46等測量器,算出作 、‘、、、置計45 υ計 使用上評電HI ^輪人燃氣輪機的熱量,並 於===算出燃氣輪機3之輸出。將燃氣 旱网枝之輸入熱量與燃氣輪播 率。^飞I枝之輪出的比稱為上述發電端效 的發埶2二方' 熱篁計45係測量乾燥狀態之燃料氣 此只要燃料氣本身之特性不變化,即使立所 3有之齡變化,測量發熱量值亦為-定。另―方/,、在 平常運轉時之燃氣輪機3的 甘纯Ii 寻&制係維持一定的輸出。 其釔果’由於當因某些原因使燃料 使供應燃料氣之每一單位妒竹 ‘刀牦加%即會 早位體%的發熱量降低, 增加送至燃氣輪機之燃料氣流量的控制。1社 丁 應至燃氣輪機之燃料氣的外觀 八、,、。,由於供 電量則維持於一定,因此增加,另一方面發 U此使發電端效率降低。 :由此濕分監測裳置來檢測此種發電端效率之降低, 即可查知濕分已混人燃料氣之可能性。當此發之 降低係起因於設備異常時,即可藉由進行終復:二"之 之迅速處置,來謀求作業之穩定化。又,當早4分專 燃料之拌生氣體本身的里常田,、在於作為 程來修正異常的原因。:,期:重新檢視氣體產生製 又可早期發現因拌生氣體異常所 28 -1277655 引起之設備的損傷,施以適當處理以確保安全作業之持續 進行。 ^以上說明之濕分監測裝i ’雖均以設置於燃氣輪機發 电。又備者來例$ ’但設置對象並非限定於燃氣輪機發電嗖 備。燃燒石化燃料之焚化鋼爐發電設備、燃燒氣體炼融爐 轧之焚化鍋爐發電設備、内燃機發電設備等,只要係將氣 體用作為燃料之燃燒設傷的燃料氣供應設備,㈣種類者 音可適用。 :由使用上述說明之濕分監測裝置或施行上述之 二::方法’即可於作業中檢測到設備作業中所產生之 …,只要在適當處設置複數個濕分監測裝置(例 ::照::)’則不須r查明設備中產生異常之處: 必要的h 4 °因此’可進行異常處所維修之 要勺準備,重新檢視運轉時程箄 之工程曰,…叮” 訂對作業影響最小 日私。亚可饭據此工程日程來配署人。^ 最適時機停止設備之作業、以短時 貝1構能在 方法。 了 n進订維修之設備管理 本發明之燃料氣之濕分監測裝 應設備所具備之既有機器。又,由二原理:可利用燃料氣供 因此壤分監測性能可穩定且長期間使^早純且構成簡易, 【圖式簡單說明】 圖1係例不燃氣輪機發電設備之 本發明-實施形態之燃料氣濕分監測心:,其具有設有 備。 、置的燃料氣供應設 29 、1277655 圖2係顯示燃料氣及從此燃料氣取樣之樣品之溫度變 化的圖表。 圖3係燃料氣中之水蒸氣分壓對該燃料氣溫度之變化 的水蒸氣飽和曲線。 圖4係例示燃氣輪機發電設備之配管圖,其具有設有 本發明一實施形態之濕分監測裝置的另一燃料氣供應設 備。 圖5係例示燃氣輪機發電設備之配管圖,其具有設有 • 本發明另一實施形態之濕分監測裝置的燃料氣供應設備。 圖6係例示燃氣輪機發電設備之配管圖,其具有設有 本發明另一實施形態之濕分監測裝置的燃料氣供應設備。 圖7係例示燃氣輪機發電設備之配管圖,其具有設有 本發明另一實施形態之濕分監測裝置的燃料氣供應設備。 ' 圖8係例示燃氣輪機發電設備之配管圖,其具有設有 ' 本發明另一實施形態之濕分監測裝置的燃料氣供應設備。 【主要元件符號說明】 ® 1,24,31 濕分監測裝置 2,23 燃料氣供應設備 _ 3 燃氣輪機 4 燃氣輪機發電設備 . 5 氣體供應配管 6 .電氣集塵器 7 氣體加熱器 8 低壓壓縮機 30 •1277655And the mass flow rate of the sample gas is the calculated mass flow rate from the sample gas production = drainage, and α is the estimated margin (bribe (four). The above I and Gs are set by the gas supply piping 5 to be saturated with water vapor. The temperature and pressure on the downstream side of the electric energy device 6 are steamed according to the steaming method shown in Fig. 3. As an example of the measuring method of the flow rate, so-called water level control can be employed. For example, the bottom of the drain container 18 is continuously controlled by the control device 20. The opening degree of the discharge valve 25 maintains the water level of the drain container 18 constant, and the drain flow rate is calculated from the opening degree of the drain valve 25. Alternatively, the discharge valve 25 at the bottom of the drain capacity = 18 is intermittently opened to make the drain container The water level of 18 is maintained at _, and the drainage flow rate is calculated from the valve opening cycle. # Any other suitable measurement method can be used. On the other hand, the flow rate of the sample gas can be set in the orifice of the gas extraction pipe. The pressure difference between the front and rear of the throttle member 16 is calculated. This stipulation can use the pressure gauges 26, 27 of the existing fuel gas supply device provided in the gas turbine power generating device 4. This pressure gauge is shown in Fig. i, usually The dust gauge 26 placed on the inlet side of the low pressure compressor 8 and the pressure gauge 27 disposed on the inlet side of the high pressure pressure 24 1277655 reducer 10. The two pressure gauges 26, 27 are separated from the cleaning member 16, but due to a pressure from The pressure loss between the inlet 27 of the throttle member 丨6 and the pressure loss between the outlet of the throttle member 16 and the other pressure gauge 26 is comparable to the differential pressure immediately before and after the throttle member 16. It is small, so the measurement of these pressure gauges is regarded as the pressure immediately after the throttling member, so that the gas flow is unobstructed. Thus, the existing machine can be used to monitor the moisture in the fuel gas. Of course, a pressure gauge for calculating the gas flow rate may be separately disposed at a position immediately before and after the throttle member 16, or a liquid pressure gauge (raanoraeter) may be used. Further, the drainage flow rate may be measured, that is, the flow rate value based on the measurement result may be calculated. The water vapor partial pressure in the fuel gas at that time. As a result, it is also possible to judge the water vapor in the fuel gas at the time in the gas supply pipe 5 which is initially set to the saturation state according to the steam meter shown in FIG. Is it actually And steam, or to what extent, wet steam. Figure 7 is the same equipment as the gas turbine power plant* shown in Figure}, 6 this gas turbine power plant 4 is equipped with the moisture monitoring device 1 of Figure i The same wetness is the k-measuring device 3 i. This wet-spot monitoring device i η is a cold-sinking device that is specially designed for the wetness of the crotch and the heating device mixed into the fuel gas. The heating device is a device that uses a liquid heat medium, so that the above-mentioned thirst is divided into six, the eyes are strong, and the iron is placed, and the 3 1 can be said to be a device for detecting that the heat medium leaks into the fuel gas. The gas heater 7, the intercooler 9 and the gas cooler 13 of the helium supply device 2 are shown, and are supplied to the liquid heat medium according to the % table, that is, As shown, the heat 25 罾 1277655 ® ® tube 32 of all devices 7, 93 is constructed as a closed circuit. The piping for cooling medium (hereinafter referred to as "heat medium circulation piping" 32 is connected (four) to the heat medium tank 33 to which the heat medium is added. The heat medium tank 33 is connected to a heat medium for the heat medium tank, and the heat medium supply pipe 34 is provided with a flow stop adjustment valve 35. The liquid level 彳% is installed in the heat medium tank 33. The control (4) is set to 20, and the stop valve 35 of the heat medium supply pipe W is switched according to the measurement result of the liquid level meter 36 to control the liquid level position in the heat medium tank 33 to control the amount of the heat medium to be maintained. Accordingly, other known measuring devices that can detect the amount of heat medium in the heat medium tank 33 are not limited to the liquid level meter. Water can be used as the heat medium. The symbol 37 indicates a hot county for the circulation pipe 32. The symbol 38 is a heat medium cooler for cooling the heat medium of the circumstance. In the present embodiment, the heat medium is supplied to the intercooler 9 and the gas cooler 13 in addition to the cooler for the heat medium. Thereafter, it is circulated while being supplied to the gas cooling heat pump 37, but is supplied to the intermediate cooling: the heat medium of the main ♦ 丄丨卯 9 is heated in the sputum fuel gas and sent to the gas The fuel gas on the heater side is heated. In this way, the swims are not lost due to leakage, etc., and the loops are circulated in the above coolers and heaters. In this case, the liquid level of the medium tank 33 does not change. When the cooling = the heat exchanger 7, the intermediate cooling 11 9 , and the gas sample 33 ... leaked into the fuel gas, the heat medium tank is replenished from the inside to the heat medium to the heat medium circulation pipe 32. The liquid level in A will temporarily decrease. After receiving the liquid level reduction signal 26 1277655 from the liquid level meter 36, the control of the dream medium circulation pipe L βρ will open the stop flow 35 to replenish the heat medium to the heat to send the invitation. The control device 2〇 is also based on the liquid level lowering signal and p oe AL becomes /#,,, and the knife is set to 3, and the thirst is divided into the fuel 翕φ沾7 from one·,,, Knife /, $ can be this. Or, you can also use the η knee wealth, the old charge to the heat medium cycle IT according to the temperature of each single valve of the stop valve 35 used to heat the media Time to send out the 彳... When the mother's early position _ is replaced by the stop valve... 'Although the flow adjustment valve is used to value the big day..., the change of the valve opening degree can be measured, and when the opening degree is larger than the predetermined value, it is issued. Fig. 8 shows another, crystal measurement 1 set. Fig. 8 shows that the system is connected with the Μ Μ 发电 发电 发电 发电 又 又 又 又The moisture monitoring device is configured to be used in a measuring device that is conventionally placed in an existing power generating device 4, and the efficiency of the power generation terminal calculated from the measurement result is 曰3. The change is used to judge the change of moisture in the fuel gas. Figure 8 shows the oxygen recording in ^, ,, and ritual branches in more detail. This gas turbine power generation is set at 4 〒, although the gas turbine 3, high pressure _ & · soil & The % machine 1 〇, the low-pressure compressor 8 and the generator 42 are connected coaxially, and the # a J glaze is not limited thereto. The compressors 8 and 10 may be disposed away from the gas turbine 3, and may be driven by another. The source is driven. The figure shows the air compressor 43 and the burner 44 of the gas wheel ^ l wish money 3. The above-mentioned wetness monitoring device is usually used for the damage of the brake field. 4, the fuel oxygen on the gas supply pipe 5 (5) 虱 / the meter 15 , the calorie meter for measuring the calorific value of the fuel gas (heat of combustion) , m , θ ... 45, used to measure the fuel gas flow The flow meter 46, and the generator 49 + * native, % % 42 The power generation output meter 47. The above-mentioned calorimeter 45 measures the heat of the squeezing knife that has removed the moisture (the dry state) fuel 27! 277655 milk heat. Another aspect, the 泠 揪. , Lian Li L δ 10 46 series measurement of the machine containing the moisture. The igniting rolling thermometer 15 is located near the exit of the § 呌Μ 包 包 轧 木 § § § , , , , , , , 4 4 4 可 可 可 可 可 可 可 可 可It is disposed at any position near the inlet of the burner 44. The flow meter 46 should be in the piping 5 and the downstream side of the machine where the moisture is mixed into the gas. By using a measuring instrument such as the existing fuel gas temperature 46, the heat of the HI-wheeled gas turbine is calculated, and the output of the gas turbine 3 is calculated at ===. The input heat and gas rotation rate of the gas-fired net branch. ^The ratio of the fly I branch is called the above-mentioned power generation end effect. The two-party 'thermal meter 45' measures the fuel gas in the dry state. As long as the characteristics of the fuel gas itself do not change, even if it is 3 years old. Change, the measured calorific value is also determined. In addition, the purely Ii finder system of the gas turbine 3 maintains a certain output during normal operation. The result is that, for some reason, the fuel is supplied to each unit of the fuel gas, and the % of the fuel is reduced, which reduces the amount of heat generated by the early body, thereby increasing the control of the flow of the fuel gas to the gas turbine. 1社丁 The appearance of fuel gas to the gas turbine 八,,,. Since the power supply is maintained at a certain level, it is increased, and on the other hand, the power generation efficiency is lowered. : The moisture is monitored to detect the decrease in the efficiency of the power generation terminal, and the possibility that the moisture component has been mixed with the fuel gas can be ascertained. When this reduction is caused by an abnormality of the equipment, it is possible to stabilize the operation by performing the final re-processing of the second " In addition, in the early 4 minutes, the mixed gas of the special fuel itself is in the field, and it is used as a reason to correct the abnormality. :, Period: Re-examine the gas generation system. Early detection of damage caused by the mixing gas abnormality 28 -1277655, and appropriate treatment to ensure the continued operation of safe operation. ^ The moisture monitoring device i' described above is installed in the gas turbine. In addition, the example is $', but the setting object is not limited to the gas turbine power generation equipment. Incineration steel furnace power generation equipment for burning fossil fuels, power plant for burning incinerators for combustion gas refining furnaces, power generation equipment for internal combustion engines, etc., as long as the gas is used as a fuel gas supply device for burning combustion of fuel, (4) . : By using the above-mentioned wetness monitoring device or by performing the above two:: method ', it is possible to detect the occurrence of equipment in the operation of the equipment... as long as a plurality of moisture monitoring devices are set at appropriate places (Example: photo ::)' Then it is not necessary to find out the abnormalities in the equipment: The necessary h 4 ° Therefore 'can prepare for the abnormal position maintenance, re-examine the operation time 箄, 叮 ” Japanese private. Yako rice is assigned to the staff according to the schedule of the project. ^ The most suitable time to stop the operation of the equipment, the short-term shell structure can be used in the method. The equipment management of the n-order maintenance and maintenance of the fuel gas moisture monitoring of the present invention The two devices are equipped with the same principle: the fuel gas can be used, so the monitoring performance of the soil can be stabilized and the structure is simple and long-term, and the composition is simple, and the structure is simple. The invention relates to a fuel gas moisture monitoring core according to an embodiment of the present invention, which has a fuel gas supply device 29 and 1277655. FIG. 2 shows a temperature of a fuel gas and a sample sampled from the fuel gas. Fig. 3 is a water vapor saturation curve of a change in water vapor partial pressure in a fuel gas to a temperature of the fuel gas. Fig. 4 is a piping diagram illustrating a gas turbine power generating apparatus having a wet body provided with an embodiment of the present invention. Another fuel gas supply device of the monitoring device is shown in Fig. 5. Fig. 5 is a piping diagram of a gas turbine power generation apparatus having a fuel gas supply device provided with a wetness monitoring device according to another embodiment of the present invention. Fig. 6 is a diagram showing gas turbine power generation. A piping diagram of a device having a fuel gas supply device provided with a moisture component monitoring device according to another embodiment of the present invention. Fig. 7 is a piping diagram showing a gas turbine power generation device having a moisture component provided with another embodiment of the present invention. Fig. 8 is a piping diagram illustrating a gas turbine power generation apparatus having a fuel gas supply apparatus provided with a moisture separation monitoring apparatus according to another embodiment of the present invention. [Main Symbol Description] ® 1 ,24,31 wet separation monitoring device 2,23 fuel gas supply equipment _ 3 gas turbine 4 gas turbine power generation equipment. 5 gas supply Piping 6. Electrical dust collector 7 Gas heater 8 Low pressure compressor 30 • 1277655

9 中間冷卻器 10 高壓壓縮機 11 回流管 12, 35 止流閥 13 氣體冷卻器 14 氣體抽取配管 15 燃料氣溫度計 16 節流構件 17 樣品氣體冷卻器 18 排水容器 19 樣品氣體溫度計 20 控制裝置 21 冷卻水供應配管 22 流量調整閥 25 排出閥 26,27 壓力計 32 熱媒循環配管 33 熱媒槽 34 熱媒供應配管 36 液面計 37 熱媒泵 38 熱媒用冷卻器 42 發電機 43 空氣壓縮機 31 ^ 1277655 44 燃燒器 45 熱量計 46 流量計 47 發電輸出計 50 燃料壓縮機 51 定量泵9 Intercooler 10 High pressure compressor 11 Return pipe 12, 35 Stop valve 13 Gas cooler 14 Gas extraction pipe 15 Fuel gas thermometer 16 Throttle member 17 Sample gas cooler 18 Drainage vessel 19 Sample gas thermometer 20 Control device 21 Cooling Water supply piping 22 Flow regulating valve 25 Discharge valve 26, 27 Pressure gauge 32 Heat medium circulation piping 33 Heat medium tank 34 Heat medium supply piping 36 Level meter 37 Heat medium pump 38 Heat medium cooler 42 Generator 43 Air compressor 31 ^ 1277655 44 Burner 45 Calorimeter 46 Flowmeter 47 Power Generation Output Meter 50 Fuel Compressor 51 Quantitative Pump

3232

Claims (1)

-1277655 十、申請專利範圍·· 1 · 一種燃料氣之渴公g>u — ”、 測裒置,係設置於燃料氣供應 口又備 其特徵在於,具有: 氣體抽取裝置,择勒_ 係對供應至燃料氣供應 一部分進行取樣;以及 …枓矾 濕分檢測裝置,係用以使以該氣體抽取裝置取樣之氣 體的昼力成為與供應至燃料氣供應設備之燃 飽和壓力大致相同的壓力,*你兮接产 …乳 亚使4樣品氣體之溫度成為供 應至燃料氣供應設備之姆 γ …、料虱之水瘵氣飽和溫度附近的溫 度,藉此檢測由該樣品氣體產生之凝結水。 2·如申請專利範圍第Μ之燃料氣之濕分監測裝置, ,中’該燃料氣供應設備,具備藉由液體熱媒來加熱燃料 氣之加熱裝置或冷卻之冷卻裝置的至少一裝置; 該氣體抽取裝置係從該加熱裝置或冷卻裝置之下游側 進行燃料氣取樣。 3·如申請專利範圍帛1項之燃料氣之濕分監測裝置, 攀其中’該濕分檢測裝置,具備: 氣體溫度檢測器,係設置於燃料氣供應設備中燃料氣 - 被設定為水蒸氣飽和狀態的燃料氣通路; - ^體壓力調節裝置,们吏以該氣體抽取裝置取樣之氣 .體壓力’成為與該氣體溫度檢測器之檢測溫度的水蒸氣飽 和壓力大致相同的壓力; 氣體溫度調節裝置,係用以使與水蒸氣飽和壓力大致 相同之壓力的該取樣氣體溫度,成為該氣體溫度檢測器之 33 1277655 檢測溫度附近的溫度;以及 凝結水偵測器,係檢測來自該樣品氣體之凝結水 4·如申請專利範圍帛3項之燃料氣之濕分監測裳置, 其中,該氣體壓力調節裝置,係使樣品氣體之壓力 蒸氣飽和壓力; 4 7jC 該氣體溫度調節裝置,係使樣品氣體溫度成為較^ 體温度檢測器之檢測溫度高既定值的溫度; 乳 該凝結水積測器,可檢測出是否有從樣品氣 結水。 /坡 5.如申請專利範圍第3項之燃料氣之濕分監測裝置, 其中,該氣體壓力調節裂置,係使樣品氣體 : 蒸氣飽和壓力; 刀&為水 呑亥氣體溫度調筋缺罢 又^即衣置,係使樣品氣體溫度成為較哕 體溫度檢測器之檢測溫度低既定值的溫度; "〃 的產=水她,可檢測出從樣:氣體產生之凝結水 ”6::申二^圍…之燃料氣之濕_^ 冉T $虱體壓力調節梦 即衣置係由形成於燃料氣之敗揭捅 路之節流構件構成的減壓構件。 7 7·如申請專利範圍第4項之燃料氣之 其中,設有複數组成斜+ 4〆 …刀里成1衣置’ 是数、,且成對之該氣體溫度 測器,各氣俨-疮% ~ 丨衣罝與减結水伯 ”版/皿度凋郎裝置,係將被該 調整為一定壓力之样口尸 版/土力凋即裝置 力之I印氣體調整為互異的溫度。 8· 一種燃料氣之渴分於 …、现成1衣置,係设於燃料氣供應設 34 1277655 備,該鱗粗* …、竹虱供應設備具備以液體熱媒加 應通路之m刀熱w通於燃料供 至少一者,^氧的加熱裝置、及用以冷卻之冷卻裝置中的 其特徵在於,具備: 冷卻::循環通路’係使液體熱媒循環於所有加熱裝置或 及.......召谷為,係將熱媒供應至該熱媒循環通路;以 ’、、,、媒祆測裝置,係檢測該熱媒貯留容器内之熱媒量· 從力ΓΓ亥熱媒檢測裝置之檢測結果,來伯側熱媒是里否有 加熱衣置或冷卻裝置浅漏至燃料氣供應通路内。 至姆=種燃料氣之濕分監測方法’係監測作為燃料供應 至九、、k狄備之氣體的濕分,其特徵在於,包含: 氣體抽取步驟,係對所供應之燃料氣一部分進行取樣; d壓力溫度調節步驟,係使所取樣之氣體的壓力成為與 所供應之燃料氣的水蒸氣飽和壓力大致相同的壓力,並成 為所供應之燃料氣的水蒸氣飽和溫度附近的溫度;以及 凝結水檢測步驟,係檢測成為上述壓力及溫 氣體所產生之凝結水; 依據该凝結水檢測結果來監測燃料氣之濕分。 10.如申請專利範圍g 9項之燃料氣之濕分監測方法, 其中’该麼力溫度調整步驟,包含: 氣體溫度檢測步驟,係檢測設定為水蒸氣飽和狀態之 燃料氣的溫度; 氣體壓力調節步驟,係使該氣體抽取步驟中取樣之氣 35 1277655 恤的[力《為與该氣體溫度檢測步驟巾所檢測之温度的 水蒸氣飽和壓力為大致相同的壓力;以及 虱體溫度調節步驟,係使該氣體抽取步·驟中取樣之氣 體的溫度,成為與該氣體溫度檢測步驟中所檢測之溫度附 近的溫度。 . n.如申請專利範圍第ι〇項之燃料氣之濕分監測方 法,其中,於該氣體壓力調節步驟中,使樣品氣體壓力成 為水蒸氣飽和壓力; • 於該氣體溫度調節步驟中,使樣品氣體溫度成為較該 氣體溫度檢測步驟中之檢測溫度高既定值的溫度; 於該凝結水檢測步驟中,檢測是否有從樣品氣體產生 凝結水,藉此來監測濕分。 1 2·如申請專利範圍第1 〇項之燃料氣之濕分於 •、v滅》則方 ^ 法,其中,於該氣體壓力調節步驟中,使樣品氣體承 ; 為水蒸氣飽和壓力; 於該氣體溫度調節步驟中,使樣品氣體溫度成為# Β 氣體溫度檢測步驟中之檢測溫度低既定值的溫度; 人 於該凝結水檢測步驟中,檢測出來自樣品氣體> 孓凝結 " 水量,藉此來監測濕分。 十一、圖式: 如次頁 36-1277655 X. Patent application scope · · · A fuel gas thirst g>u — ”, measuring device, is installed in the fuel gas supply port and is characterized in that it has: a gas extraction device, Sampling a portion supplied to the fuel gas supply; and ... the wetness detecting device is configured to cause the pressure of the gas sampled by the gas extracting device to be substantially the same as the burning saturation pressure supplied to the fuel gas supplying device , * You pick up the product... The temperature of the sample gas of the milk is made to the temperature near the saturation temperature of the water 瘵 ..., the material of the fuel gas supply device, thereby detecting the condensed water produced by the sample gas. 2. The method of claim 1, wherein the fuel gas supply device comprises at least one device for heating a fuel gas by means of a liquid heat medium or a cooling device for cooling; The gas extraction device performs fuel gas sampling from the downstream side of the heating device or the cooling device. 3. The fuel gas moisture as claimed in the patent scope 帛1 The monitoring device, which is equipped with the 'humidity detecting device, has: a gas temperature detector, which is set in the fuel gas supply device, the fuel gas is set to a fuel gas passage in a state of water vapor saturation; - ^ body pressure regulating device,气 The gas sampled by the gas extraction device has a pressure that is substantially the same as the water vapor saturation pressure of the gas temperature detector; the gas temperature adjustment device is configured to be substantially the same as the water vapor saturation pressure. The temperature of the sample gas of the pressure becomes the temperature near the detection temperature of 33 1277655 of the gas temperature detector; and the condensate detector detects the condensed water from the sample gas. 4. The fuel gas of the patent application 帛3 item The moisture monitoring device is disposed, wherein the gas pressure adjusting device is configured to make the sample gas pressure vapor saturation pressure; 4 7jC The gas temperature adjusting device is such that the sample gas temperature becomes higher than the detection temperature of the body temperature detector. The value of the temperature; milk condensate detector, can detect whether there is water from the sample gas. / Slope 5. The fuel gas moisture monitoring device according to item 3 of the patent application scope, wherein the gas pressure regulating cracking is performed to make the sample gas: vapor saturation pressure; the knife & Moreover, the clothes are placed so that the sample gas temperature becomes a temperature lower than the detection temperature of the carcass temperature detector; "〃 production=water she can detect the sample: the condensed water produced by the gas” 6: : Shen 2 ^ circumference ... fuel gas wet _ ^ 冉 T $ 虱 body pressure adjustment dream that the clothing is a decompression member formed by the throttle member formed in the fuel gas failure road. 7 7·If the fuel gas of the fourth paragraph of the patent application scope is provided, the complex composition is inclined + 4 〆... The knives are made into a garment, the number is, and the pair of gas temperature detectors, each gas 俨 - Sore% ~ 丨 罝 减 减 减 减 减 ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” ” 8· A fuel gas thirst is divided into..., ready-made 1 garment, set in the fuel gas supply set 34 1277655, the scale is thick* ..., the bamboo raft supply equipment has the m-knife heat added by the liquid heat medium The utility model is characterized in that: the heating device for supplying at least one of the fuel, the heating device for the oxygen, and the cooling device for cooling are characterized in that: the cooling: the circulation passage is configured to circulate the liquid heat medium to all the heating devices or. ..... 召谷, is to supply the heat medium to the heat medium circulation path; to detect the amount of heat medium in the heat medium storage container by ',,,, media testing device The detection result of the medium detecting device, whether the heating medium in the primary side is heated or the cooling device leaks to the fuel In the gas supply path, the moisture distribution monitoring method for the fuel gas is used to monitor the moisture content of the gas supplied as fuel to the gas, and includes: a gas extraction step, which is supplied Part of the fuel gas is sampled; d. The pressure temperature adjustment step is such that the pressure of the sampled gas becomes substantially the same pressure as the water vapor saturation pressure of the supplied fuel gas, and becomes the vicinity of the water vapor saturation temperature of the supplied fuel gas. And the condensed water detecting step detects the condensed water generated by the pressure and the warm gas; and monitors the moisture content of the fuel gas according to the condensed water detecting result. 10. If the fuel gas of the patent scope g 9 is applied a moisture monitoring method, wherein the 'moisture temperature adjustment step comprises: a gas temperature detecting step of detecting a temperature of a fuel gas set to a water vapor saturation state; and a gas pressure adjusting step of sampling the gas in the gas extraction step 35 1277655 [The force of water vapor saturation pressure for the temperature detected by the gas temperature detection step towel is The same pressure is applied; and the temperature adjustment step of the body is such that the temperature of the gas sampled in the gas extraction step is the temperature near the temperature detected in the gas temperature detecting step. The method for monitoring a moisture content of a fuel gas according to the item ,, wherein, in the gas pressure adjusting step, the sample gas pressure is a water vapor saturation pressure; • in the gas temperature adjusting step, the sample gas temperature is made to be higher than the gas The temperature in the temperature detecting step is a temperature at which the detected temperature is higher than a predetermined value; in the condensed water detecting step, it is detected whether or not condensed water is generated from the sample gas, thereby monitoring the moisture content. 1 2 If the patent application scope is the first item The moisture of the fuel gas is divided into:, v, and then the method, wherein in the gas pressure adjusting step, the sample gas is carried; the water vapor saturation pressure; in the gas temperature adjusting step, the sample gas temperature is made # 温度 The temperature at which the detected temperature in the gas temperature detecting step is lower than the predetermined value; in the condensed water detecting step, the human detects the Product gas > relic coagulation " water, whereby the moisture is monitored. XI. Schema: as the next page 36
TW094137125A 2005-10-19 2005-10-24 Fuel gas moisture monitoring apparatus and method of monitoring fuel gas moisture TWI277655B (en)

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KR100958939B1 (en) 2010-05-19
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WO2007046139A1 (en) 2007-04-26
KR20080040748A (en) 2008-05-08

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