JPS5951112A - Lng heat utilized generating set - Google Patents
Lng heat utilized generating setInfo
- Publication number
- JPS5951112A JPS5951112A JP16090382A JP16090382A JPS5951112A JP S5951112 A JPS5951112 A JP S5951112A JP 16090382 A JP16090382 A JP 16090382A JP 16090382 A JP16090382 A JP 16090382A JP S5951112 A JPS5951112 A JP S5951112A
- Authority
- JP
- Japan
- Prior art keywords
- lng
- medium
- condenser
- evaporator
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
Abstract
Description
【発明の詳細な説明】
本発明は、I、NO冷熱利用発電装回に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a power generation system using I, NO cold energy.
従来の、中間熱媒体(以下媒体と略−ツ−)を用いたラ
ンキンサイクルを第1図に示す。第1図において1は媒
体凝縮器(以下凝縮器と略ず)、2は媒体ボンフ、3は
媒体蒸発器、4は媒体タービン、5はハG蒸発器、6は
LNG流貴調節弁である。また、媒体蒸発器3およびL
NG蒸発器5を流れる熱#、 6it体は+’frt水
であるが、海水温度は季節によって変化する。ここで媒
体蒸発器3に着目すると、設計点としていかなる海水温
度を選択するのが最適かという事が問題となる。今仮に
夏場と冬場との中間的な海水温度において媒体、1<発
器ff:設計した場合ケ考えると冬場に〃σ水渦ルニが
づ↓X5下し定時、媒体蒸発器の蒸発能力が不足するの
で、I、No流すを減らず事によって媒体流話を減少さ
せなけれはならない。しかし一般にLNG 、%i熱利
用光亀装餞の下流にはNoを燃料とする火力発゛屯所や
都市ガス供給設備が控えているのでこの様な操作はNo
の安定供給の見地から1−ると非相に不都合な闇である
。また、LNG 3iL量を減らす様な事態ケ回M′N
−るためには、媒1$ 1g発器を、最低の海水gL度
でも余裕をもって蒸発できるように十分大きく設治しな
けれはならない。しかし媒体蒸発器がプラント全体に占
めるコスl及びスペースの割合は非雷に犬であり、この
様な股引では設飢スペースの点がらも、またコスト的に
も冷発プラント全体として大変無駄である。FIG. 1 shows a conventional Rankine cycle using an intermediate heat medium (hereinafter simply referred to as the medium). In Fig. 1, 1 is a medium condenser (hereinafter abbreviated as condenser), 2 is a medium bomb, 3 is a medium evaporator, 4 is a medium turbine, 5 is a H-G evaporator, and 6 is an LNG flow control valve. . Also, medium evaporator 3 and L
The heat flowing through the NG evaporator 5 is +'frt water, but the seawater temperature changes depending on the season. Focusing on the medium evaporator 3, the question is what seawater temperature is optimal to select as a design point. Now, if the medium is designed at an intermediate seawater temperature between summer and winter, 1 < generator ff. Considering this, in winter, if σ water vortex is lowered by ↓X5 at a fixed time, the evaporation capacity of the medium evaporator is insufficient. Therefore, it is necessary to reduce media flow without reducing I, No flow. However, in general, there are thermal power plants and city gas supply facilities that use NO as fuel downstream of LNG and %i heat utilization optical systems, so such operations are not recommended.
From the standpoint of stable supply of gas, this is an extremely inconvenient darkness. In addition, there will be times when the amount of LNG will be reduced by 3iL.
In order to do so, the generator must be large enough to evaporate even the lowest gL of seawater with a margin. However, the proportion of cost and space that the medium evaporator occupies in the entire plant is unmatched, and this arrangement is extremely wasteful for the entire refrigeration plant, both in terms of installation space and cost. .
本発明はこの様な事情に鑑みてなされ7コものであり、
その目的とするところは、少ない製造コスト、あるいは
建設スペースで年間を通じてNG全安定供給できるLN
G冷熱利用発電装置な提供1〜ることにある。The present invention has been made in view of these circumstances, and has seven aspects:
The aim is to provide LN with a stable supply of NG throughout the year with low manufacturing costs or construction space.
The first thing to be done is to provide a power generation device using cold energy.
本発明の一実施例を図面を用いて以下に説明す、る。第
2図において1は媒体凝縮器、2は媒体ポンプ、3は媒
体蒸発器、4は媒体タービン、5はLNG蒸発器、6
J−j I、NG流量調節弁、7はLNG術圧ポンプ、
8はLNG圧力調節弁である。An embodiment of the present invention will be described below with reference to the drawings. In FIG. 2, 1 is a medium condenser, 2 is a medium pump, 3 is a medium evaporator, 4 is a medium turbine, 5 is an LNG evaporator, and 6
J-j I, NG flow control valve, 7 is LNG surgical pressure pump,
8 is an LNG pressure control valve.
本発明は上記招成より成るものであり、その作用を第3
図を用いて以下に説明する。第31匂は凝縮器l内のL
NGの状態を等圧線を用いて示した曲線図であり、縦軸
はLNGのエンタルピ、横軸はLNGの温度、Pl、P
tはLNG圧力(Pt>p+)である。The present invention consists of the above-mentioned features, and its effects can be summarized as follows.
This will be explained below using figures. The 31st odor is L in the condenser l
It is a curve diagram showing the state of NG using isobar lines, the vertical axis is the enthalpy of LNG, and the horizontal axis is the temperature of LNG, Pl, P.
t is the LNG pressure (Pt>p+).
またT、は凝縮器1の入口LNG温度、T2は凝縮器1
の出口LNG温度、T、は媒体凝縮温度である。LNG
の圧力がPlの如く低い場合は、凝縮器1の内部でのL
NGのエンタルピ久化翔、はム■とカリ、ここでLNG
流量をGとすると、媒体の凝縮のために使われるLNG
N熱冷はG×△Iで表わされる。一方、LNGの圧力が
Ptの如く旨い場合は、凝RM器内でのLNGのに使わ
れるLNG冷熱り七はG×Δ■′となる。Also, T is the inlet LNG temperature of condenser 1, and T2 is condenser 1
The exit LNG temperature, T, is the medium condensation temperature. LNG
When the pressure of is as low as Pl, L inside the condenser 1
NG's enthalpy Kukasho, Ham■ and Kali, LNG here
If the flow rate is G, LNG used for condensing the medium
N hot/cool is expressed as G×△I. On the other hand, when the pressure of LNG is high like Pt, the LNG cooling and heating temperature used for LNG in the condensing RM device becomes G×Δ■′.
ここで、ランキンライフル奢流れる奴体の7H7p6は
、媒体の凝縮器に等しく、媒体の凝縮1には媒体の凝i
NIMのために使われるLNG i賃熱桁に比例する。Here, 7H7p6 of the Rankin rifle flowing body is equal to the medium condenser, and the medium condensation 1 has the medium condensation i
It is proportional to the amount of LNG used for NIM.
従ってLN()の圧力を制御することによって間接的に
媒体の流量を制御することが可能である事がわかる。す
なわち、冬場に海水温度が低く女(ハ媒体蒸発器3の蒸
発能力が低下した時は、LNGの圧力を高くして媒体の
流量が少なくなる様に制御J−れは、LN(+を定格流
5量流し続けることが可能と々る。Therefore, it can be seen that by controlling the pressure of LN(), it is possible to indirectly control the flow rate of the medium. In other words, in winter, when the seawater temperature is low and the evaporation capacity of the medium evaporator 3 decreases, the LNG pressure is increased and the flow rate of the medium is reduced. It is possible to continue flowing 5 volumes of water.
なお、第2図に示す実施例に於ては、LNG圧力が1℃
節ブ[8がLNG蒸発器5の下L′flL側にある場合
を示しているが、本発明はLNG圧力圧力2井1とLN
G蒸発器5との中間にある場合にも適用できる。In the example shown in FIG. 2, the LNG pressure is 1°C.
Although the case where the node [8] is located on the L'flL side below the LNG evaporator 5 is shown, the present invention
It can also be applied to the case where it is located between the G evaporator 5 and the G evaporator 5.
以上の様に本発明によると、媒体凝(支)器の下流側の
LNG配管にLNG Fi:力調節Jrケ設り、媒体蒸
発器の蒸発能力即ち海水温厩とLNGの流量−に応じて
凝縮器内のLNG圧力を調節することによって、より少
ないコスト、より狭い設置スペースで年間上進じて略一
定量のNG送気か継続できるLNG冷熱利用発電装置を
実」、できるという効果がある。As described above, according to the present invention, LNG Fi: force adjustment Jr. is installed in the LNG piping on the downstream side of the medium condenser (support), and the LNG Fi: force adjustment Jr. By adjusting the LNG pressure in the condenser, it is possible to create a power generation system using LNG cold energy that can continue to supply a substantially constant amount of NG air every year at lower costs and in a smaller installation space. .
第1図は従来のランキンサイクルを示す系統図、第2図
は本発明の一実施例を示す系統図、第3図は凝縮器内の
LNGの挙動を説明するための曲線図である。
1・・媒体凝縮器、2・・・媒体ポンプ、3・・・媒体
蒸発器、4・・・媒体タービン、5・・・LNG蒸発器
、6・・・LNG流M.M節介、7・・・LNG !イ
圧ポンプ、8・LN(J圧力調節弁、(7317)代理
人ブl′理士 側近 廂、佑 (目か1名)シ毎水
第1図
第2図
第3図FIG. 1 is a system diagram showing a conventional Rankine cycle, FIG. 2 is a system diagram showing an embodiment of the present invention, and FIG. 3 is a curve diagram for explaining the behavior of LNG in a condenser. 1... Medium condenser, 2... Medium pump, 3... Medium evaporator, 4... Medium turbine, 5... LNG evaporator, 6... LNG flow M. M Sesuke, 7...LNG! A pressure pump, 8・LN (J pressure control valve, (7317) Agent Bl' Physician, close aide, Yu (eye or 1 person) Shi every water
Figure 1 Figure 2 Figure 3
Claims (1)
いそのLNG i海水を熱源とする熱交換器で気化した
後送気するLNG冷熱利用発電システムにおいて、LN
G配管に海水温度に応じて前記凝縮器内LNGの圧力調
節機能を有する調節弁を設けることを特徴とする丑G冷
熱利用発電装置。In a power generation system using LNG cold energy, LNG is used as a cold heat source for the condenser of the Rankine cycle.
A power generation device utilizing cold energy in the UshiG cold energy system, characterized in that the G pipe is provided with a control valve having a function of regulating the pressure of the LNG in the condenser according to the seawater temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16090382A JPS5951112A (en) | 1982-09-17 | 1982-09-17 | Lng heat utilized generating set |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16090382A JPS5951112A (en) | 1982-09-17 | 1982-09-17 | Lng heat utilized generating set |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5951112A true JPS5951112A (en) | 1984-03-24 |
Family
ID=15724831
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16090382A Pending JPS5951112A (en) | 1982-09-17 | 1982-09-17 | Lng heat utilized generating set |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5951112A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009136916A1 (en) * | 2008-05-07 | 2009-11-12 | Utc Power Corporation | Active stress control during rapid shut down |
US11083109B2 (en) * | 2017-06-21 | 2021-08-03 | Hongfujin Precision Electronics (Tianjin) Co., Ltd. | Heat exchange system |
-
1982
- 1982-09-17 JP JP16090382A patent/JPS5951112A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009136916A1 (en) * | 2008-05-07 | 2009-11-12 | Utc Power Corporation | Active stress control during rapid shut down |
US11083109B2 (en) * | 2017-06-21 | 2021-08-03 | Hongfujin Precision Electronics (Tianjin) Co., Ltd. | Heat exchange system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6279312B1 (en) | Gas turbine with solar heated steam injection system | |
US4094147A (en) | Circuit for the supply of condensable fluid to a solar engine | |
JPS5951112A (en) | Lng heat utilized generating set | |
JP2001081484A (en) | Liquefied-gas evaporation apparatus with cold-heat generation function | |
WO2020110473A1 (en) | Boiler system, power generation plant, and boiler system operation method | |
JPS6045328B2 (en) | heating device | |
JP5721408B2 (en) | Hot spring water supply system and hot spring water supply method | |
JP2002089790A (en) | Lpg vaporizing mechanism | |
ES8606619A1 (en) | Air conditioning plant using a heat pump with a static exterior heat exchanger and with dry vapour regulation by automatically changing the rate of flow through the expansion valve. | |
KR0146008B1 (en) | Absorptive air-conditioner with boiler having advanced heat efficiency | |
JPH03242429A (en) | Gas turbine plant | |
WO2019187894A1 (en) | Liquefied natural gas vaporization system | |
JPH0471142B2 (en) | ||
JPS6113546B2 (en) | ||
JPS58135308A (en) | Cold temperature power plant | |
JPS6157923B2 (en) | ||
JPS61235685A (en) | Temperature control device in waste heat retrieving device for thermal plant | |
JPS6049197A (en) | Circulating flow control unit of thermosyphon reboiler | |
JPS6149586B2 (en) | ||
JPH1114007A (en) | Reheat steam temperature controller of boiler | |
JP2002364941A (en) | Absorption refrigerating unit and its operation method | |
JPS60117069A (en) | Refrigerator with double bundle type condenser | |
JPS5832927A (en) | Gas turbine device | |
JPS6065211A (en) | Operating method for lng coldness power generating plant | |
JPS58173355A (en) | Absorption type heat pump device |