JPH0633863B2 - Open rack type vaporizer with underwater burner - Google Patents
Open rack type vaporizer with underwater burnerInfo
- Publication number
- JPH0633863B2 JPH0633863B2 JP24512988A JP24512988A JPH0633863B2 JP H0633863 B2 JPH0633863 B2 JP H0633863B2 JP 24512988 A JP24512988 A JP 24512988A JP 24512988 A JP24512988 A JP 24512988A JP H0633863 B2 JPH0633863 B2 JP H0633863B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- seawater
- burner
- water
- 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.)
- Expired - Fee Related
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
- F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0382—Constructional details of valves, regulators
- F17C2205/0385—Constructional details of valves, regulators in blocks or units
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0135—Pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0408—Level of content in the vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0636—Flow or movement of content
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Description
【発明の詳細な説明】 利用産業分野 この発明は、オープンラック型気化装置の散水系の改良
に係り、循環貯水槽、海水を昇温する水中バーナー槽、
所定温度まで昇温する混合槽及び散水器への循環ポンプ
からなる循環系水路を設けて、高負荷及び非常用の予備
機を不要にした水中バーナー付きオープンラック型気化
装置に関する。Description: TECHNICAL FIELD The present invention relates to an improvement of a watering system of an open rack type vaporizer, and relates to a circulating water storage tank, an underwater burner tank for heating seawater,
The present invention relates to an open rack type vaporizer with a submersible burner that does not require a high load and an emergency standby machine by providing a circulation system water passage consisting of a mixing tank for raising a temperature to a predetermined temperature and a circulation pump to a sprinkler.
背景技術 液化天然ガス(以下LNGという)を気化させる装置とし
て、オープンラック型気化装置(以下ORVという)が多
用されている。ORVは第6図に示す如く、例えば、多数
のフィン付きチューブを上下一対のヘッダータンク(1)
(2)にて並列配置した熱交換パネル(3)に、上部より下部
へ熱媒体たる海水を流下させる散水器(4)を付設し、揚
水ポンプ(5)にて海水を散水器(4)へ送水する構成からな
り、熱交換パネル(3)内を上昇するLNGと海水とを熱交換
させて、これを気化させる。BACKGROUND ART As a device for vaporizing liquefied natural gas (hereinafter referred to as LNG), an open rack type vaporizer (hereinafter referred to as ORV) is often used. As shown in FIG. 6, the ORV has, for example, a large number of finned tubes and a pair of upper and lower header tanks (1).
A heat exchanger panel (3) arranged in parallel in (2) is equipped with a sprinkler (4) for flowing down seawater as a heat medium from the upper part to the lower part, and a pump for pumping seawater to sprinkle the seawater (4). It is configured to send water to and heats LNG rising in the heat exchange panel (3) and seawater to vaporize it.
海水を熱源とするORVは、その設計に際し、LNG負荷100
%、海水温度ミニマムの条件で設計され、また、熱交換
パネルへ散水する海水の送水量は、前記設計条件に拘ら
ず必要な量を一定制御する構成からなる。When designing an ORV that uses seawater as a heat source, the LNG load of 100
%, The seawater temperature is designed under a minimum condition, and the amount of seawater to be sprayed to the heat exchange panel is controlled so that the necessary amount is constantly controlled regardless of the design conditions.
従って、海水温度が設計値を下回ると能力が低下するた
め、ガス供給量を最大となすピークロード時あるいは非
常時に供えて、第7図に示す如く、貯水槽(6)内にLNGが
流れる熱交換コイル(8)を内蔵させ、配設する水中バー
ナー(7)の燃焼熱で気化させる構成からなる、所謂サブ
マージドベーパーライザー(以下SMVという)とよばれ
る水中燃焼型気化装置を予備機として付設するのが一般
的であった。Therefore, if the seawater temperature falls below the design value, the capacity will decrease, so that the heat of LNG flowing in the water tank (6) can be used as shown in Fig. 7 during peak load when the gas supply amount is maximum or during an emergency. A submerged combustion vaporizer called so-called submerged vaporizer (SMV), which has a built-in exchange coil (8) and is vaporized by the combustion heat of the submerged burner (7), is installed as a standby unit. It was common to do.
従来技術の問題点 従来のORVは、前記予備機を設置するため、建設費が増
大し、かつ多大の設置スペースを要するなどの問題があ
るほか、送水量が一定に制御されることから、通常運転
時では過剰送水しており、運転費に無駄があった。Problems with the conventional technology Conventional ORVs have the problems of increased construction cost and large installation space due to the installation of the above-mentioned standby machine. During operation, excess water was supplied, resulting in wasted operating costs.
かかる問題から、ORVには、需要ピーク時の如き一時的
ピークロードや低海水温度時の能力確保のため、設置に
多大のコストとスペースを要する予備機を用いる構成よ
りも、たとえ運転費が一時的に増大しても、多大の設置
スペースを必要としない構成が切望されている。Because of this problem, the ORV has a higher operating cost than the configuration that uses a spare machine that requires a large amount of cost and space for installation in order to secure capacity during temporary peak loads such as during peak demand and at low seawater temperatures. There is a strong demand for a configuration that does not require a large installation space even if the number of devices increases.
また、通常運転時はLNG負荷及び海水温度に見合った送
水量を供給でき、電力量の削減を図ることができるORV
が切望されている。Also, during normal operation, it is possible to supply an amount of water that is commensurate with the LNG load and seawater temperature, and reduce the amount of electricity used.
Is coveted.
発明の目的 この発明は、かかる現状に鑑み、予備機のSMVを必要と
せず、一時的なピークロードにも容易に対応でき、通常
運転時には最適温度、量の海水を送給できる構成からな
るORVの提供を目的としている。SUMMARY OF THE INVENTION In view of the present situation, the present invention is an ORV that does not require an SMV of a standby machine, can easily cope with a temporary peak load, and can supply seawater of optimum temperature and amount during normal operation. The purpose is to provide.
発明の概要 この発明は、熱交換パネル内を上昇するLNGを散水器よ
り散水する海水にて熱交換を気化させるオープンラック
型気化装置において、 揚水された海水及び熱交換パネルに散水後の海水を貯水
しかつ排水系を有する貯水槽と、 水中バーナーを付設して海水を昇温するバーナー槽と、 バーナー槽からの高温海水と貯水槽からの海水を混合し
所定温度に昇温させる混合槽と、 貯水槽からの海水をバーナー槽と混合槽とに振分けて流
下させる流量制御手段と、 混合槽からの海水を散水器へ送水するため循環ポンプを
付設したポンプ槽、 を有した海水の循環系水路を備えたことを特徴とする水
中バーナー付きオープンラック型気化装置である。SUMMARY OF THE INVENTIONThe present invention is an open rack type vaporizer that evaporates heat exchange with seawater sprinkling LNG rising in a heat exchange panel from a water sprinkler, in which pumped seawater and seawater after being sprinkled on the heat exchange panel are used. A water storage tank that stores water and has a drainage system, a burner tank that is equipped with an underwater burner to heat seawater, and a mixing tank that mixes high-temperature seawater from the burner tank and seawater from the water storage tank to raise the temperature to a predetermined temperature. , A seawater circulation system having flow control means for distributing the seawater from the water storage tank to the burner tank and the mixing tank and flowing it down, and a pump tank equipped with a circulation pump for sending the seawater from the mixing tank to the sprinkler. It is an open rack type vaporizer with an underwater burner characterized by having a water channel.
発明の構成 この発明による水中バーナー付きオープンラック型気化
装置は、以下の構成を特徴とする。Configuration of the Invention The open rack type vaporizer with an underwater burner according to the present invention is characterized by the following configurations.
一時的ピークロードや低海水温度時には、水中バーナ
ーを用いて海水温度を所要温度まで上昇させて能力を確
保し、予備機のSMVを不要にする。During temporary peak loads and low seawater temperatures, an underwater burner is used to raise the seawater temperature to the required temperature to ensure capacity, and the spare SMV is unnecessary.
一方、揚水する海水温度が所要温度よりも高い場合、
循環ポンプを使用して熱媒体の海水の一部を循環利用す
る。循環利用に際し、熱交換パネルへ散水され熱交換後
の海水温度を検知し、揚水した海水と混合して所定温度
まで昇温させてから所要量を供給するように制御する。On the other hand, if the temperature of the pumped seawater is higher than the required temperature,
A part of seawater as a heat carrier is circulated using a circulation pump. At the time of recycling, the temperature of seawater after being sprinkled on the heat exchange panel and after heat exchange is detected, the temperature is mixed with the pumped seawater to raise the temperature to a predetermined temperature, and then a required amount is supplied.
また、熱交換前の海水温度を基準にこれを一定に制御す
ることもできる。Further, the seawater temperature before heat exchange can be controlled to be constant based on the seawater temperature.
水中バーナー使用にともなう海水の酸性化を、比較的
小容積のバーナー槽にて燃焼させることにより、水温を
高温に維持して海水中への燃焼ガスの溶解を減少させて
いる。By burning the acidification of seawater due to the use of an underwater burner in a burner tank of a relatively small volume, the water temperature is maintained at a high temperature and the dissolution of combustion gas in seawater is reduced.
循環系水路において、揚水ポンプによる補給水、水中
バーナーの燃焼により発生する水にて増量し、系内の各
槽の水面が上昇するが、所要温度の海水を貯水し送水す
るためのポンプ槽の水面レベルに応じて、貯水槽より排
水するか、あるいは貯水槽からオーバーフローさせるた
め、加熱した海水をすてることがなく、循環系内の海水
量と熱量を所定量に制御する。In the circulation system water channel, the amount of water supplemented by a pump and the water generated by the combustion of an underwater burner increases, and the water level of each tank in the system rises.However, a pump tank for storing and sending seawater at the required temperature is used. Depending on the water level, water is drained from the water tank or overflowed from the water tank, so that the heated seawater is not drained, and the amount of seawater and heat in the circulation system are controlled to a predetermined amount.
また、この発明において、貯水槽からの海水をバーナー
槽と混合槽とに振分けて流下させる流量制御手段は、ポ
ンプと三方弁を用いた構成とするほか、水頭差落下構成
の水槽配列となし、バーナー槽と混合槽への流下振分け
量を、貯水槽下流側に設けたスライド堰、あるいは貯水
槽に設けた水中堰、浮子式堰を組合せることにより制御
することができる。Further, in the present invention, the flow rate control means for distributing the seawater from the water storage tank to the burner tank and the mixing tank and flowing it down is configured to use a pump and a three-way valve, and is also a water tank arrangement having a head drop structure, The amount of flow distribution to the burner tank and the mixing tank can be controlled by combining a slide weir provided on the downstream side of the water storage tank, an underwater weir provided at the water storage tank, or a floating weir.
この発明において、バーナー槽の高温海水と貯水槽から
バイパスされる低温海水は混合槽で所定温度に混合され
るが、散水器へ循環送水するためのポンプ槽内で、海水
を所定温度に混合できる場合はこの混合槽を省略しても
よい。In the present invention, the high temperature seawater in the burner tank and the low temperature seawater bypassed from the water storage tank are mixed to a predetermined temperature in the mixing tank, but the seawater can be mixed to a predetermined temperature in the pump tank for circulating water to the sprinkler. In this case, this mixing tank may be omitted.
発明の図面に基づく開示 第1図はこの発明による水中バーナー付きオープンラッ
ク型気化装置の全体構成を示す水槽と管路の説明図であ
る。Disclosure Based on Drawings of the Invention FIG. 1 is an explanatory view of a water tank and a pipeline showing the entire configuration of an open rack type vaporizer with an underwater burner according to the present invention.
第2図はこの発明による水中バーナー付きオープンラッ
ク型気化装置の貯水槽等の各槽の構成を示す斜視説明図
である。第3図は第2図における溢水の水頭差を示す貯
水槽とスライド堰の縦断説明図である。FIG. 2 is a perspective explanatory view showing the configuration of each tank such as a water tank of the open rack type vaporizer with a submersible burner according to the present invention. FIG. 3 is a vertical cross-sectional explanatory view of the water storage tank and the slide weir showing the difference in head of overflow water in FIG.
第4図と第5図は貯水槽と流下流量の制御手段の種々構
成を示す縦断説明図である。4 and 5 are longitudinal explanatory views showing various configurations of the water storage tank and the flow-down flow rate control means.
第1図に示す水中バーナー付きオープンラック型気化装
置の貯水槽(10)は、熱交換パネル(3)の下方に配置さ
れ、散水器(4)からの溢水して熱交換パネル(3)にそって
落下しながら降温した海水を受けて貯留し、その底部に
は排水口が設けられ、排水制御バルブ(11)が設けてあ
る。The water tank (10) of the open rack type vaporizer with a submersible burner shown in Fig. 1 is arranged below the heat exchange panel (3), and overflows from the sprinkler (4) into the heat exchange panel (3). The seawater, which has fallen in temperature while falling, is received and stored, and a drain port is provided at the bottom thereof and a drain control valve (11) is provided.
また、貯水槽(10)には、揚水ポンプ(5)から供給される
海水も貯留される。なお、この供給海水は通常運転中、
排水口から排水されない位置に供給される。Further, seawater supplied from the pumping pump (5) is also stored in the water storage tank (10). In addition, this seawater supply during normal operation,
It is supplied from the drain to a position where it is not drained.
この貯水槽(10)に隣接して、水中バーナー(12)が配設さ
れたバーナー槽(13)が設けられ、さらにバーナー槽(13)
からの溢水が流入する混合槽(14)が下流側に設けてあ
る。A burner tank (13) provided with an underwater burner (12) is provided adjacent to this water storage tank (10), and further a burner tank (13)
A mixing tank (14) into which the overflow water flows is provided on the downstream side.
この混合槽(14)からの溢水は下流側のポンプ槽(15)に入
ったのち、循環ポンプ(16)にて散水器(4)に送水され
る。The overflow water from the mixing tank (14) enters the pump tank (15) on the downstream side and is then sent to the sprinkler (4) by the circulation pump (16).
熱交換パネル(3)より貯水槽(10)に落下してきた冷たい
海水は、揚水ポンプ(5)で新たに取り入れられた海水に
て昇温する。The cold seawater that has fallen from the heat exchange panel (3) to the water storage tank (10) is heated by the seawater newly taken in by the pumping pump (5).
揚水ポンプ(5)からの流入量は、前記の落下海水温度を
検知する制御器(20)がバルブ(21)を介して、落下海水温
度に応じて制御し、また、該制御器(20)は水中バーナー
(12)の燃焼制御弁(22)の開閉をも制御する。なお、図中
の23は水中バーナー(12)のブロワーである。The inflow amount from the pumping pump (5) is controlled by the controller (20) for detecting the temperature of the falling seawater according to the temperature of the falling seawater via the valve (21), and the controller (20). Underwater burner
It also controls the opening and closing of the combustion control valve (22) of (12). Reference numeral 23 in the figure is a blower for the underwater burner (12).
貯水槽(10)の海水は、バーナー槽(13)内海水温度を検知
する制御器(19)にて開閉制御される三方弁(17)を介し
て、バーナー槽(13)と混合槽(14)に振り分けられ、かつ
所要量がポンプ送給される。また、貯水量を越える冷た
い海水は槽底部の排水口より排出される。The seawater in the water storage tank (10) is passed through a burner tank (13) and a mixing tank (14) via a three-way valve (17) that is controlled to open and close by a controller (19) that detects the seawater temperature in the burner tank (13). ), And the required amount is pumped. In addition, cold seawater that exceeds the storage amount is discharged from the drain port at the bottom of the tank.
また、この排水制御バルブ(11)は、ポンプ槽(15)の水面
レベルを検出する検知器(18)にて、水面レベルに応じて
開閉制御される。The drainage control valve (11) is controlled to open / close according to the water surface level by a detector (18) that detects the water surface level of the pump tank (15).
上記の構成において、熱交換後の海水温度を検知し、こ
れを一定に制御するため、揚水ポンプ(5)の負荷は所要
気化に必要な熱量分だけとなり、ポンプ動力の電力量を
削減できる。In the above configuration, the seawater temperature after heat exchange is detected and controlled to be constant, so that the load of the pumping pump (5) is only the amount of heat necessary for the required vaporization, and the amount of power for pump power can be reduced.
また、貯水槽(10)からの海水の分配は、各槽の配置を以
下に示す水頭差落下式に配置することにより行われる
が、分配ポンプを用いる方法でもよい。Further, the distribution of seawater from the water storage tank (10) is performed by arranging the tanks in a head drop manner described below, but a method using a distribution pump may be used.
第2図に示す水槽は、貯水槽(10)の一方壁上部端に移動
自在のスライド堰(30)を設け、このスライド堰(30)の両
側からの溢水が、それぞれ隣接するバーナー槽(13)、混
合槽(14)に流入するよう、さらにバーナー槽(13)から混
合槽(14)にも流入するよう、各槽壁高さを調整してあ
り、最後に混合槽(14)からポンプ槽(15)に流入する構成
からなる。The water tank shown in FIG. 2 is provided with a movable slide weir (30) at the upper end of one wall of the water storage tank (10), and overflow water from both sides of the slide weir (30) is adjacent to the burner tank (13). ), The height of each tank wall is adjusted so that it flows into the mixing tank (14) and further into the mixing tank (14) from the burner tank (13), and finally the pump is pumped from the mixing tank (14). It is configured to flow into the tank (15).
前記スライド堰(30)は、貯水槽(10)からの海水をバーナ
ー槽(13)と混合槽(14)とに振分けて流下させ、また、そ
のスライド位置により各槽への流量を制御することがで
きる。The slide weir (30) distributes the seawater from the water storage tank (10) to the burner tank (13) and the mixing tank (14) and allows it to flow down, and controls the flow rate to each tank by the slide position. You can
また、貯水槽(10)は、第3図に示す如く、スライド堰(3
0)を設けた壁と、その対向位置の他壁高さを適宜選定す
ることにより水面を一定化できる。すなわち、(hB-ho)
を適切値に選定すると、バーナー槽(13)と混合槽(14)に
流入する水量がほぼ一定し、余分な海水は他壁よりオー
バーフローして排出される。Further, the water tank (10) has a slide weir (3
The water surface can be made constant by appropriately selecting the height of the wall provided with (0) and the height of the other wall at the opposite position. In other words, (h B -h o)
When is selected as an appropriate value, the amount of water flowing into the burner tank (13) and the mixing tank (14) becomes almost constant, and excess seawater overflows from the other wall and is discharged.
流量の安定制御する手段として、第4図に示す如く、水
中堰(31)を貯水槽(10)に設けることができ、液面の変化
に対する安定性が高く、貯水槽(10)からバーナー槽(13)
と混合槽(14)に流入する水量がより安定する。As a means for stabilizing the flow rate, as shown in FIG. 4, an underwater weir (31) can be provided in the water storage tank (10), which is highly stable against changes in the liquid level and can be used from the water storage tank (10) to the burner tank. (13)
And the amount of water flowing into the mixing tank (14) becomes more stable.
また、第4図において、水中堰(31)をスライドさせる構
成とすることもできる。Further, in FIG. 4, the underwater weir (31) may be slid.
さらに、第5図に示す如く、貯水槽(10)を仕切壁(32)に
て2分し、この仕切壁(32)上流側に、一対の浮子(33)と
これに挾持された堰(34)からなる浮子式堰を設けること
により、主たる貯水槽(10)の水面に応じて浮子式堰が動
き、水面の絶対レベルによらずにhBが一定となり、流量
が一定になる。Further, as shown in FIG. 5, the water storage tank (10) is divided into two parts by a partition wall (32), and a pair of floats (33) and a weir held by the float (33) are provided upstream of the partition wall (32). By providing the float type weir consisting of 34), the float type weir moves according to the water surface of the main water storage tank (10), h B becomes constant regardless of the absolute level of the water surface, and the flow rate becomes constant.
また、仕切壁を設けることなく浮子式堰をスライド堰(3
0)の直前に配置することもできる。In addition, the float type weir slides without a partition wall (3
It can be placed just before (0).
発明の効果 この発明による水中バーナー付きオープンラック型気化
装置は、以下の効果を有する。Effects of the Invention The open rack type vaporizer with a submersible burner according to the present invention has the following effects.
一時的オーバーロードや低海水温度時に対応でき、予
備機のSMVが不要となり、設置スペースを小さくでき
る。It can cope with temporary overload and low seawater temperature, does not require the SMV of the standby machine, and can reduce the installation space.
熱交換後の海水温度を検知しこれを一定に制御するた
め、循環ポンプの負荷は所要気化に必要な熱量分だけと
なり、ポンプ動力の電力量を削減できる。Since the seawater temperature after heat exchange is detected and controlled constantly, the load on the circulation pump is limited to the amount of heat required for the required vaporization, and the amount of power for pump power can be reduced.
また、熱交換後の海水温度を一定に制御する方法の他、
ポンプ槽内の海水温度を一定に制御することもでき、同
様に、ポンプ動力の電力量を削減できる。In addition, other than the method of controlling the seawater temperature after heat exchange to be constant,
The seawater temperature in the pump tank can be controlled to be constant, and similarly, the amount of power for pump power can be reduced.
海水送水系が故障時は、水中バーナーと循環海水系の
みで運転が可能となる。When the seawater delivery system fails, it can be operated only by the underwater burner and the circulating seawater system.
水中バーナー使用時の循環海水をバーナー槽とこれを
バイパスする槽とに分流させ、その後合流混合し所要温
度となすため、過剰な加熱をすることなく水の酸性化防
止ができ、省エネルギーと装置の防蝕が達成できる。Circulating seawater when using an underwater burner is split into a burner tank and a tank that bypasses it, and then combined and mixed to reach the required temperature, so acidification of water can be prevented without excessive heating, which saves energy and equipment. Corrosion protection can be achieved.
第1図はこの発明による水中バーナー付きオープンラッ
ク型気化装置の全体構成を示す水槽と管路の説明図であ
る。 第2図はこの発明による水中バーナー付きオープンラッ
ク型気化装置の貯水槽等の各槽の構成を示す斜視説明図
である。第3図は第2図における溢水の水頭差を示す貯
水槽とスライド堰の縦断説明図である。 第4図と第5図は貯水槽と流下流量の制御手段の種々構
成を示す縦断説明図である。 第6図は従来のオープンラック型気化装置の構成を示す
説明図であり、第7図は併設されるサブマージドベーパ
ーライザーの構成を示す説明図てある。 1,2……ヘッダータンク、3……熱交換パネル、4……
散水器、5……揚水ポンプ、10……貯水槽、11……排水
制御弁、12……水中バーナー、13……バーナー槽、14…
…混合槽、15……ポンプ槽、16……循環ポンプ、17……
三方弁、18……検知器、19,20……制御器、21……バル
ブ、22……燃料制御弁、23……ブロワー。FIG. 1 is an explanatory view of a water tank and a pipeline showing the overall configuration of an open rack type vaporizer with an underwater burner according to the present invention. FIG. 2 is a perspective explanatory view showing the configuration of each tank such as a water tank of the open rack type vaporizer with a submersible burner according to the present invention. FIG. 3 is a vertical cross-sectional explanatory view of the water storage tank and the slide weir showing the difference in head of overflow water in FIG. 4 and 5 are longitudinal explanatory views showing various configurations of the water storage tank and the flow-down flow rate control means. FIG. 6 is an explanatory diagram showing the configuration of a conventional open rack type vaporizer, and FIG. 7 is an explanatory diagram showing the configuration of a submerged vaporizer to be installed side by side. 1,2 …… Header tank, 3 …… Heat exchange panel, 4 ……
Sprinkler, 5 ... Pumping pump, 10 ... Water tank, 11 ... Drainage control valve, 12 ... Underwater burner, 13 ... Burner tank, 14 ...
… Mixing tank, 15 …… Pump tank, 16 …… Circulation pump, 17 ……
Three-way valve, 18 ... Detector, 19,20 ... Controller, 21 ... Valve, 22 ... Fuel control valve, 23 ... Blower.
フロントページの続き (72)発明者 小池 健介 千葉県君津郡袖ケ浦町福王台3―4 (72)発明者 錦織 稔 千葉県富津市笹毛48 (72)発明者 佐藤 洋治 兵庫県尼崎市西長洲本通2丁目6番地 住 友精密工業株式会社内 (72)発明者 庄谷 仁延 兵庫県尼崎市西長洲本通2丁目6番地 住 友精密工業株式会社内Front page continuation (72) Kensuke Koike 3-4 Fukuodai, Sodegaura-cho, Kimitsu-gun, Chiba Prefecture Minoru Nishiki Minoru 48 Sasage, Futtsu-shi, Chiba Prefecture (72) Yoji Sato Nishi-Nagamoto-dori, Amagasaki-shi, Hyogo Prefecture 2-6, Sumitomo Precision Industries Ltd. (72) Inventor, Hitonobu Shoya 2-6, Nishi-Nagasuhondori, Amagasaki City, Hyogo Prefecture Sumitomo Precision Industries Ltd.
Claims (2)
散水器より散水する海水にて熱交換し気化させるオープ
ンラック型気化装置において、揚水された海水及び熱交
換パネルに散水後の海水を貯水しかつ排水系を有する貯
水槽と、水中バーナーを付設して海水を昇温するバーナ
ー槽と、バーナー槽からの高温海水と貯水槽からの海水
を混合し所定温度に昇温させる混合槽と、貯水槽からの
海水をバーナー槽と混合槽とに振分けて流下させる流量
制御手段と、混合槽からの海水を散水器へ送水するため
循環ポンプを付設したポンプ槽、を有した海水の循環系
水路を備えたことを特徴とする水中バーナー付きオープ
ンラック型気化装置。1. An open rack type vaporizer for heat-vaporizing and liquefying liquefied natural gas rising in a heat exchange panel with seawater sprinkled from a sprinkler, wherein the pumped seawater and the sprinkled seawater are heat-exchanged on the heat exchange panel. A water storage tank that stores water and has a drainage system, a burner tank that is provided with an underwater burner to heat seawater, and a mixing tank that mixes high-temperature seawater from the burner tank and seawater from the water storage tank and raises the temperature to a predetermined temperature. , A seawater circulation system having a flow rate control means for distributing the seawater from the water storage tank to the burner tank and the mixing tank and flowing it down, and a pump tank provided with a circulation pump for sending the seawater from the mixing tank to the sprinkler An open rack type vaporizer with an underwater burner, which is equipped with a water channel.
または混合槽、ポンプ槽へ、順次、水頭差にて流下し、
かつ不要海水が貯水槽より溢水する構成からなることを
特徴とする第1項記載の水中バーナー付きオープンラッ
ク型気化装置。2. Sea water from a water tank is used as a burner tank and / or
Or, it flows down to the mixing tank and the pump tank one by one with a head difference,
The open rack type vaporizer with an underwater burner according to claim 1, characterized in that unnecessary seawater overflows from the water storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24512988A JPH0633863B2 (en) | 1988-09-29 | 1988-09-29 | Open rack type vaporizer with underwater burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24512988A JPH0633863B2 (en) | 1988-09-29 | 1988-09-29 | Open rack type vaporizer with underwater burner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0293200A JPH0293200A (en) | 1990-04-03 |
| JPH0633863B2 true JPH0633863B2 (en) | 1994-05-02 |
Family
ID=17129059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24512988A Expired - Fee Related JPH0633863B2 (en) | 1988-09-29 | 1988-09-29 | Open rack type vaporizer with underwater burner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0633863B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100888394B1 (en) * | 2007-07-05 | 2009-03-13 | 한국가스공사 | Expansion Optimization Method of LGN Vaporization System |
| WO2022180810A1 (en) * | 2021-02-26 | 2022-09-01 | 日揮株式会社 | Fuel gasification equipment |
| WO2022180812A1 (en) * | 2021-02-26 | 2022-09-01 | 日揮株式会社 | Fuel vaporization equipment |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6478699B2 (en) * | 2015-02-25 | 2019-03-06 | 住友精密工業株式会社 | Underwater combustion type vaporizer |
| KR102217227B1 (en) * | 2020-12-07 | 2021-02-18 | 주식회사 태진중공업 | Seawater supply device for open rack vaporizer |
-
1988
- 1988-09-29 JP JP24512988A patent/JPH0633863B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100888394B1 (en) * | 2007-07-05 | 2009-03-13 | 한국가스공사 | Expansion Optimization Method of LGN Vaporization System |
| WO2022180810A1 (en) * | 2021-02-26 | 2022-09-01 | 日揮株式会社 | Fuel gasification equipment |
| WO2022180812A1 (en) * | 2021-02-26 | 2022-09-01 | 日揮株式会社 | Fuel vaporization equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0293200A (en) | 1990-04-03 |
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