JPS61287404A - Collecting device for coagulatory material - Google Patents

Collecting device for coagulatory material

Info

Publication number
JPS61287404A
JPS61287404A JP12797285A JP12797285A JPS61287404A JP S61287404 A JPS61287404 A JP S61287404A JP 12797285 A JP12797285 A JP 12797285A JP 12797285 A JP12797285 A JP 12797285A JP S61287404 A JPS61287404 A JP S61287404A
Authority
JP
Japan
Prior art keywords
cooling
heating
collector
gas
coagulatory
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP12797285A
Other languages
Japanese (ja)
Other versions
JPH0128601B2 (en
Inventor
Teruo Ishikubo
石窪 照男
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Power Reactor and Nuclear Fuel Development Corp
Original Assignee
Mitsubishi Heavy Industries Ltd
Power Reactor and Nuclear Fuel Development Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd, Power Reactor and Nuclear Fuel Development Corp filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12797285A priority Critical patent/JPS61287404A/en
Publication of JPS61287404A publication Critical patent/JPS61287404A/en
Publication of JPH0128601B2 publication Critical patent/JPH0128601B2/ja
Granted legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To improve performance for feeding coagulatory material to a collecting and recovering device by providing a cooling unit serving also as a heating unit contg. a coolant generating system and a heat medium generating system connected to a compressor to each collecting device for the coagulatory material. CONSTITUTION:Coagulatory gas generated in a generating device N1 is fed to a cooling/heating collector A11 by opening an introducing value V1 at the generating side N11 of the gas wherein a heating surface a11 is held at cold condition by cooling previously with a coolant fed from a cooling/heating unit B11. Thus, the coagulatory gas is collected by being cooled and coagulated. When the collector A11 is filled fully by the coagulated material, the introducing value V1 is closed and the introducing valve V6 is opened and the coagulatory gas is introduced into the cooling/heating collector A12 from a gas generating side N12, and the coagulatory gas is collected similarly. During this collecting operation using the collector A12, collected coagulatory gas is transferred to a receiving vessel D11 in the system of the collector A1.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、凝結性ガスの発生装置に連結され前記ガスを
冷却して捕集しかつ加熱して回収容器等へ供給する複数
の冷却・加熱型捕集器を有し、該捕集器の冷却・加熱機
構に特徴を有する凝結性物質の捕集装置に関するもので
ある。
Detailed Description of the Invention (Industrial Field of Application) The present invention provides a plurality of cooling systems connected to a condensable gas generator to cool and collect the gas, heat it, and supply it to a collection container or the like. The present invention relates to a collection device for condensable substances that has a heating type collector and is characterized by a cooling/heating mechanism of the collector.

(従来の技術) 凝結性物質(ナフタリン、ベンゼン等)の前記捕集装置
の従来例は、第8図に示すように凝結性ガスの発生装置
(プラント−図示省略)に連結(並列)された複数の冷
却・加熱型捕集器(A)に、加熱源(ハ)を有する熱交
換器(B)から供給される熱媒を主管(3)、分岐管(
Xl)(X2)(X3)を経て前記捕集器(勾のそれぞ
れに供給して循環する加熱ユニットと、冷却源停)を有
する熱交換器(C)から供給される冷媒を主管(イ)、
分岐管(Yl)(Y2)(Y3)を経て前記捕集器(A
)のそれぞれに供給して循環する冷却ユニットを連結し
、前記捕集器(A)の前後配管および前記ユニット間の
配管に開閉弁を配設して、1個の冷却ユニットによって
全ての前記捕集器(A)に冷媒を供給し導入される凝結
性ガスを冷却、凝結させて捕集するとともに、1個の加
熱ユニットによって全ての前記捕集器(A)に熱媒を供
給し捕集された凝結性物質を融解または昇華させて回収
容器等に供給して回収する構造になっており、複数より
なる前記捕集器(A)群は、前記発生装置において連続
的に発生する凝結性ガスを連続的に捕集できるようにな
っている。
(Prior Art) A conventional example of the collection device for condensable substances (naphthalene, benzene, etc.) is connected (in parallel) to a condensable gas generator (plant - not shown) as shown in Fig. 8. The heat medium supplied from the heat exchanger (B) having the heating source (C) is transferred to the plurality of cooling/heating type collectors (A) through the main pipe (3) and the branch pipe (
Xl) (X2) (X3) The refrigerant supplied from the heat exchanger (C) having the collector (a heating unit that supplies and circulates to each gradient, and a cooling source stop) is supplied to the main pipe (A). ,
The collector (A) passes through branch pipes (Yl) (Y2) (Y3).
), and opening/closing valves are provided in the front and rear piping of the collector (A) and the piping between the units, so that all the traps can be handled by one cooling unit. A refrigerant is supplied to the collector (A) to cool, condense and collect the introduced condensable gas, and a heat medium is supplied to all the collectors (A) and collected by one heating unit. The structure is such that the collected coagulable substances are melted or sublimated and then supplied to a collection container or the like for recovery. It is designed to capture gas continuously.

(従来技術の問題点) 従来の凝結性物質の捕集装置においては、複数の冷却・
加熱型捕集器に対し、1個の冷却ユニットと1個の加熱
ユニットとを共通に設けているため、各1個の冷却源お
よび加熱源が大容量となり、特に、低温冷却時における
冷却源の冷凍能力が3トン以上に達し、高圧ガス保安規
則による年1回の開放点検のために、該点検時に全ての
前記捕集器の運転停止即ちプラント全体の停止を余儀な
くされ、プラント稼働率が著しく低下される。
(Problems with the conventional technology) In the conventional collection device for condensable substances, multiple cooling and
Since a heating type collector is provided with one cooling unit and one heating unit in common, each cooling source and heating source have a large capacity, especially when cooling at low temperatures. The refrigeration capacity of the plant has reached over 3 tons, and due to the annual open inspection required by the High Pressure Gas Safety Regulations, all of the collectors have to be stopped, that is, the entire plant has to be shut down, resulting in a drop in plant availability. Significantly reduced.

また、前記の状態を回避するためには、前記捕集器ごと
に冷却ユニットと加熱ユニットを併設することが必要と
なり、各種機器および配管ループの二重化とともに交互
の切換え運転が必要であるなど、著しく構造が複雑化し
コスト高になり経済的に大きい負担となる。
In addition, in order to avoid the above situation, it is necessary to install a cooling unit and a heating unit for each collector, which requires duplication of various equipment and piping loops, and alternate switching operation. The structure becomes complicated and the cost increases, resulting in a heavy economic burden.

さらに、冷却ユニット、加熱ユニットにおける冷却源お
よび加熱源の中間冷・熱媒体を用いて熱交換器で熱授受
を行うとともに、熱交換器から供給される冷・熱媒によ
って前記捕集器に熱授受を行う間接冷却・加熱方式にな
っているため、熱効率の低下は免れない。
Furthermore, heat is exchanged in a heat exchanger using the intermediate cooling/heating medium of the cooling source and heating source in the cooling unit and heating unit, and the cooling/heating medium supplied from the heat exchanger is used to transfer heat to the collector. Since it uses an indirect cooling/heating method that transfers electricity and receives electricity, a decrease in thermal efficiency is inevitable.

さらにまた、プラント中に点在され−(いる前記捕集器
群に対し、冷媒および熱媒の長距離輸送が必要であって
、特に、低温の冷媒輸送は、道中の吸熱によって前記捕
集器に必要な温度で送り届けられない恐れがあるため、
予め吸熱による温度上昇を見込んださらに低温の冷媒と
イる必要があり、エネルギーが浪費されるとともに、輸
送エネルギーが別に必要となる。
Furthermore, it is necessary to transport the refrigerant and heat medium over long distances to the collectors scattered throughout the plant, and in particular, the transport of low-temperature refrigerant is difficult due to the absorption of heat along the way. Because there is a risk that the product may not be delivered at the required temperature,
It is necessary to use a lower temperature refrigerant that allows for the temperature rise due to heat absorption in advance, which wastes energy and requires additional transportation energy.

前記のような欠点は、いずれも多数の前記捕集器が用い
られる大型プラントでは大きい障害となる、などの欠点
がある。
All of the above-mentioned drawbacks include the fact that they become a major hindrance in large-scale plants where a large number of the collectors are used.

(発明の目的、問題点の解決手段) 本発明は、従来の凝結性物質の捕集装置における前ロピ
のような問題点に対処するために開発されたものであっ
て、凝結性ガスの発生装置に連結された複数の冷却・加
熱型捕集器のそれぞれに、コンプレッサーに連結された
冷媒発生系と熱媒発生系とを有する冷却兼加熱ユニット
を設けた構成に特徴を有し、凝結性ガスの発生装置に複
数の冷却・加熱型捕集器を連結するとともに前記捕集器
ごとに冷却兼加熱ユニットを設けることにより、発生装
置で連続的に発生する凝結性ガスを連続的に捕集し回収
可能にするとともに、前記発生装置の運転停止をしない
で前記捕集器を個別に点検、補修可能にして稼働率を高
め、コンプレッサーニ連結された冷媒発生系と熱媒発生
系とを有する冷却兼加熱ユニットを設けたことにより、
優れた冷媒および熱媒の発生、供給機能を有しかつ大幅
な構造簡素化、コン/(クト化を可能にし凝結性物質の
捕集さらには回収装置等への供給性能を著しく向上させ
て前記のような従来の問題点を解消した凝結性物質の捕
集装置を供する点にある。
(Objective of the Invention, Means for Solving Problems) The present invention was developed in order to deal with the problems of the conventional collection devices for condensable substances. It is characterized by a configuration in which each of the plurality of cooling/heating type collectors connected to the device is provided with a cooling/heating unit having a refrigerant generation system and a heating medium generation system connected to a compressor. By connecting multiple cooling/heating type collectors to a gas generator and providing a cooling/heating unit for each collector, condensable gas continuously generated by the generator can be continuously collected. The present invention has a refrigerant generation system and a heating medium generation system that are connected to a compressor unit, and the collection device can be inspected and repaired individually without stopping the operation of the generator to increase the operating rate. By installing a cooling and heating unit,
It has excellent refrigerant and heat medium generation and supply functions, greatly simplifies the structure, enables compaction, and significantly improves the collection performance of condensable substances and the supply performance to recovery equipment, etc. The object of the present invention is to provide a collection device for condensable substances that solves the conventional problems such as.

(発明の実施例) 第1図ないし#1IJ7図に本発明の実施例を示してお
り、第1図、第2図は本発明の第1実施例であって、図
中(N1)は凝結性物質を連続的に発生する発生装置(
プラント)であって、該発生装置(N1)Kffけうi
eり2 個rl)Nス発生口(N□、)l(N、2)に
は、受入弁(Vl)、(V6)を介して冷却・加熱型捕
集器(A11 ) + (A1□)がそれぞれ連結され
ているとともに、前記冷却・加熱型捕集器(A□I)t
(AI□)には、冷却兼加熱用の伝熱面(C1、)、(
α1□)が内蔵されており、また、コンプレッサーに連
結された冷媒発生系と熱媒発生系とを有する冷却兼加熱
ユニット(B□□) 、 (B1□)が連結されて設け
られている。また、前記mi器(A11)、(A12)
 ニハ、回収弁(V2)、(V7)を介して回収容器(
D、□)、(D1□)が連結されている。
(Embodiment of the invention) An embodiment of the present invention is shown in Fig. 1 to #1IJ7, and Fig. 1 and Fig. 2 are the first embodiment of the present invention, and (N1) in the figure A generator that continuously generates sexual substances (
plant), and the generator (N1)
A cooling/heating type collector (A11) + (A1□ ) are connected to each other, and the cooling/heating type collector (A□I)t
(AI□) has a heat transfer surface (C1,) for cooling and heating, (
α1□) is built-in, and cooling/heating units (B□□) and (B1□) having a refrigerant generation system and a heat medium generation system connected to a compressor are connected. In addition, the mi device (A11), (A12)
ni, the collection container (
D, □) and (D1□) are connected.

さらに、前記冷却兼加熱ユニツ) (B1□)について
詳述すると、特に第2図に示すようにコンプレッサー(
C,)、該コンプレッサー(C’1)の吐出側に連結さ
れた冷却水管(h□)付のコンデンサー(cl)と冷媒
供給弁α3)および膨張弁α4)が一連に配設されてい
る冷媒発生系、前記コンプレッサー(C1)の吐出側、
に連結された冷却水または蒸気管(A2)付の補助冷却
・加熱器(−2)と熱媒供給弁α5)が一連に配設され
ている熱媒発生系とからなり、前記冷媒発生系と熱媒発
生系とは並列に配置されているとともに、前記両系は一
連の共通配管によって冷却・加熱型捕集器(A□、)の
伝熱面(C1□)側に連結され、該伝熱面(−11)側
から前記コンプレッサー(C1)に循環配管が連結され
た構成になっており、前記冷却兼加熱ユニット(B、□
)についても前記と同様な構成になっている。
Furthermore, the cooling/heating unit) (B1□) will be explained in detail, especially the compressor (
C,), a refrigerant in which a condenser (cl) with a cooling water pipe (h□) connected to the discharge side of the compressor (C'1), a refrigerant supply valve α3) and an expansion valve α4) are arranged in series. generation system, the discharge side of the compressor (C1);
The refrigerant generation system consists of an auxiliary cooling/heater (-2) with a cooling water or steam pipe (A2) connected to a heating medium supply valve α5), and a heating medium generation system in which a heating medium supply valve α5) is arranged in series. and the heat medium generation system are arranged in parallel, and both systems are connected to the heat transfer surface (C1□) side of the cooling/heating type collector (A□,) by a series of common piping. A circulation pipe is connected to the compressor (C1) from the heat transfer surface (-11) side, and the cooling/heating unit (B, □
) also has the same configuration as above.

(作用) 第1.2図に示した本発明の第1実施例は、前記のよう
な構成になっており、その作用について説明すると、発
生装置(N1)は、凝結性ガスを連続的に発生するプラ
ントであって、運転を開始するとその停止に際して、停
止動作、再起動のための所要時間が長(、その間の生産
量低下が著しいとか、その作業に人件費が多くかかる、
起動停止のために機械的損傷が起きやすいとかの不利益
が著しい装置であって、発生装置へ)で発生した凝結性
ガスを冷却・加熱型捕集器(A1、)に供給して捕集す
る際は、ガス発生口(N1□)側の受入弁α1)を開き
、冷却兼加熱ユニツ) (B1、)から供給されている
冷媒によって予め伝熱面(α□1)を冷却した状態で行
われ、前記捕集器(A、□)内に導入された前記凝結性
ガスは冷却され凝結、固化されて器内に捕集される。前
記捕集に際し冷却兼加熱ユニットにおいては、コンプレ
ッサー(C1)からの吐出ガス(圧縮ガス)をコンデン
サ(#1)で凝縮させ、該凝縮液は冷媒供給弁(C3)
、膨張弁(C4)を経て低温ガス即ち冷媒となり前記捕
集器(A1、)内の伝熱面(C1、)を冷却したのち循
環配管を経てコンプレッサー(C1)へ循環される冷媒
発生系の運転になっており(この間、熱媒発生系は不作
動)、通常、コンプレッサー(C1)から前記各機器を
経て循環される機構は、冷凍機と称されるものであって
その冷凍能力はコンデンサ(C1)の大きさで決まる。
(Function) The first embodiment of the present invention shown in FIG. When the plant starts operating, it takes a long time to shut down and restart (the production volume decreases significantly during that time, or the labor costs are high for the work).
It is a device that has significant disadvantages such as easy mechanical damage due to startup and stoppage, and the condensable gas generated in the generator (to the generator) is collected by supplying it to the cooling/heating type collector (A1). When doing so, open the receiving valve α1) on the gas generation port (N1□) side, and cool the heat transfer surface (α□1) in advance with the refrigerant supplied from the cooling/heating unit (B1). The condensable gas introduced into the collector (A, □) is cooled, condensed, solidified, and collected in the collector. During the collection, in the cooling and heating unit, discharge gas (compressed gas) from the compressor (C1) is condensed in the condenser (#1), and the condensed liquid is passed through the refrigerant supply valve (C3).
, a refrigerant generation system in which the low-temperature gas, that is, the refrigerant, passes through the expansion valve (C4), cools the heat transfer surface (C1,) in the collector (A1,), and is then circulated to the compressor (C1) via the circulation pipe. (during this period, the heat medium generation system is inactive), and the mechanism that circulates from the compressor (C1) through each of the above devices is called a refrigerator, and its refrigerating capacity is equal to that of the condenser. It is determined by the size of (C1).

前記捕集を続けると前記捕集器(A1□)内に捕集され
る凝結性物質が増加して満量になるため、受入弁(vl
)を閉、受入弁(C6)を開に切換えて、連続的に発生
される凝結性ガスをガス発生口(N1□)側から冷却・
加熱型捕集器(A1□)へ導入し前記と同様な作用によ
って同凝結性ガスを連続して捕集する。
If the collection is continued, the amount of coagulable substances collected in the collector (A1□) increases until it is full, so the intake valve (vl
) is closed and the intake valve (C6 is opened) to cool and cool the continuously generated condensable gas from the gas generation port (N1□) side.
The condensable gas is introduced into a heating type collector (A1□) and is continuously collected by the same action as described above.

前記捕集器(A1□)による凝結性ガスの捕集操作中に
、前記捕集器(A11)においては捕集した凝結性ガス
を回収容器(Dl、)へ送り出し同容器に回収させる。
During the operation of collecting condensable gas by the collector (A1□), the condensable gas collected in the collector (A11) is sent to the collection container (Dl,) and collected therein.

前記回収操作は回収弁(′v2)を開き冷却兼加熱ユニ
ツ) (B1.)から熱媒を供給して伝熱面(all)
を加熱し、前記捕集器(A1、)内に捕集されている凝
結固体即ち凝結性物質を融解あるいは昇華させて低圧側
の回収容器(Dl、)側へ流入させ、回収容器(Dl、
)において再び冷却して凝結、固化させるなどの手段に
よって回収し、前記捕集器(A、□)内の捕集物を払い
出して次回の捕集態勢にする。前記凝結性物質の払い出
し回収に際し冷却兼加熱ユニットにおいては、コンプレ
ッサ(C1)からの吐出ガス(通常フロンガスが使用さ
れており、圧縮高温熱媒ガスになっている。)をコンデ
ンサ(#2)によって蒸気あるいは冷却水で温度調整し
たのち所望温度の熱媒とし、該熱媒を熱媒供給弁α5)
を経て前記捕集器(A1、)内の伝熱面(α1□)VC
供給し加熱したのち循環配管を経てコンプレッサ(C1
)へ循環させる熱媒発生系の運転になっている(この間
、冷媒発生系は不作動に切換えられている)。
The recovery operation is performed by opening the recovery valve ('v2) and supplying the heat medium from the cooling/heating unit (B1) to the heat transfer surface (all).
is heated to melt or sublimate the coagulated solids, that is, coagulable substances collected in the collector (A1,) and flow into the collection container (Dl,) on the low pressure side.
), the collected material is collected by means such as cooling again to condense and solidify, and the collected material in the collector (A, □) is discharged to prepare for the next collection. When discharging and collecting the condensable substances, in the cooling/heating unit, the gas discharged from the compressor (C1) (usually Freon gas is used, and is compressed high temperature heat transfer gas) is passed through the condenser (#2). After adjusting the temperature with steam or cooling water, it is used as a heating medium at a desired temperature, and the heating medium is supplied to the heating medium supply valve α5).
through the heat transfer surface (α1□) in the collector (A1,) VC
After being supplied and heated, it is passed through the circulation piping to the compressor (C1
) is in operation (during this period, the refrigerant generation system is switched to non-operation).

前記のように発生装置(No)に対し【少くとも2個の
冷却兼加熱ユニット付冷却・加熱型捕集器(A、。)、
(A、□)組を並列に連結しているため、一方の前記捕
集器によって凝結性ガスを捕集している時に、他方の前
記捕集器では捕集した凝結性物質を払い出して回収させ
次の捕集態勢に準備できるとともに、さらに点検あるい
は部品交換等、また伝熱面の予冷時間の確保も可能とな
り、前記両捕集器(A11 ) a (”1□)の作動
切換えによって、発生装置部)から連続的に凝結性ガス
を捕集しかつ回収容器等へ払い出して回収できる。
As mentioned above, for the generator (No.) [at least two cooling/heating collectors with cooling/heating units (A, .),
(A, □) Since the sets are connected in parallel, when one of the collectors is collecting condensable gas, the other collector is discharging and collecting the collected condensable substances. By switching the operation of both collectors (A11) a ("1□), it is possible to prepare for the next collection mode, as well as to perform further inspections, parts replacement, etc., and to secure pre-cooling time for the heat transfer surface. Condensable gas can be continuously collected from the generator (generator section) and discharged into a collection container or the like for collection.

前記のように本発明の冷却兼加熱ユニット0□1)。As mentioned above, the cooling and heating unit of the present invention 0□1).

(B1□)は、前記捕集器(A11 ) e (A1□
)ごとに設けられかつ前記のような構成になっているた
め、伝熱面(−,1)、(−,2)の冷却および加熱機
能は十分に確保されるとともに、冷凍能力は3トン未満
に設計可能であり、また、凝結性ガスの捕集運転中に随
時に補修点検でき一定期間ごとの試験検査も実施できる
。日常の補修点検要領を定め習熟しておくことにより、
また随時に補修点検を実施することによって前記試験検
査が短時間で終ることになつて、2個の冷却兼加熱ユニ
ット付冷却・加熱型捕集器(A1.)、(A、2)組に
より発生装置部)の長期間無停止の稼働を期待できる。
(B1□) is the collector (A11) e (A1□
) and have the above-mentioned configuration, sufficient cooling and heating functions are ensured for the heat transfer surfaces (-, 1) and (-, 2), and the refrigeration capacity is less than 3 tons. In addition, it is possible to carry out repairs and inspections at any time during condensable gas collection operation, and to conduct tests and inspections at regular intervals. By establishing and becoming familiar with daily repair and inspection procedures,
In addition, by carrying out repair inspections from time to time, the above-mentioned test and inspection can be completed in a short time. The generator section) can be expected to operate without interruption for a long period of time.

(発明の他の実施例) 第3図に本発明の第2実施例を示しており、前記第1実
施例に比べると発生装置(N2)の第1、第2ガス発生
口(N2□) 、 (N2□)に、前記第1実施例と同
様な構成になっている冷却兼加熱ユニット0□1)付冷
却・加熱型捕集器(A2□)組と、同じく冷却兼加熱ユ
ニット(B2□)付冷却・加熱型捕集器(A2□)組と
を連結するとともに、さらに、第3ガス発生口(N2.
)に、前記第1実施例と同様な構成になっている冷却兼
加熱ユニツ) (B2.)付冷却・加熱型捕集器(A2
.)組を、予備系として連結した構成に特徴を有するも
のであって、常時、該予備系を予冷して捕集の待機状態
にすることにより、故障に際しいつでも切換操作が可能
であって信頼性をさらに向上できる。
(Other Embodiments of the Invention) FIG. 3 shows a second embodiment of the present invention, in which the first and second gas generation ports (N2□) of the generator (N2) are different from the first embodiment. , (N2□) includes a set of cooling/heating collectors (A2□) with a cooling/heating unit 0□1) having the same configuration as the first embodiment, and a set of cooling/heating type collectors (A2□) with the same cooling/heating unit (B2). □) is connected to the cooling/heating type collector (A2□) set, and a third gas generation port (N2.
), a cooling/heating type collector (A2.) with a cooling/heating unit (B2.) having the same configuration as the first embodiment.
.. ) is connected as a standby system, and by always pre-cooling the standby system to standby for collection, it can be switched at any time in the event of a failure, increasing reliability. can be further improved.

さらに、第4図に本発明の第3実施例を示しており、該
実施例は発生装置(Nn)のガス発生口が1個でありか
つ凝結性ガスの発生量が大量である場合に対応できるよ
うにしたものであって、前記第1実施例と同様な構成に
なっている多数の冷却兼加熱ユニット(Bi12)付冷
却・加熱型捕集器(A、、1)組、冷却兼加熱ユニット
(BrLt)付冷却・加熱型捕集器(ArLt)組、冷
却兼加熱二二ツ) (Bm、)付冷却・加熱型捕集器(
〜1)組、冷却兼加熱ユニット(垢、)付冷却・加熱型
捕集器(A4)組、さらには予備系として冷却兼加熱ユ
ニツ) (E、1)付冷却・加熱型捕集器(A、1)組
を、および冷却兼加熱ユニツ) (Bl、)付冷却・加
熱型捕集器(A、、)組を、それぞれ発生装置(Nρの
ガス発生口に受入弁を介して並列に連結した構成になっ
ており、第3実施例の特徴は、発生装置(NrL)から
発生する大量の凝結性ガスを複数の前記捕集器(A、□
)・・・(Ant)群と複数の前記捕集器(Aよ□)・
・・(Am、)群(tは個数を表示)とによって、同時
に複数の捕集器群によって捕集できかつ切換えを可能に
するとともに、複数の予備系捕集器(A11)・・・(
Al、)群を設けた構成にあり、前記各捕集器群におけ
る個数は凝結性ガスの発生蓋に対応して設定され、発生
装置のρの生産に支障を及ぼすことなく連続運転を可能
とし、さらに、随時に点検修理、定検を実施でき故障に
も十分に対処できるなど、凝結性ガスの捕集、払い出し
回収性能がさらに格段に高められ、信頼性が著しく向上
されている。
Furthermore, FIG. 4 shows a third embodiment of the present invention, which is applicable to the case where the generator (Nn) has one gas generation port and a large amount of condensable gas is generated. A set of cooling/heating type collectors (A, 1) with a number of cooling/heating units (Bi12) having the same configuration as the first embodiment, cooling/heating Cooling/heating type collector (ArLt) set with unit (BrLt), cooling/heating type collector (22) with cooling/heating unit (Bm,)
~1) set, cooling/heating type collector (A4) with cooling/heating unit (Screw), and even cooling/heating type collector (A4) with cooling/heating unit (E, 1) as a backup system A, 1) set, and a cooling/heating type collector (A,,) set with a cooling/heating unit) (Bl,) are connected in parallel to the gas generation port of the generator (Nρ) through a receiving valve. The feature of the third embodiment is that a large amount of condensable gas generated from the generator (NrL) is connected to the plurality of collectors (A,
)...(Ant) group and a plurality of said collectors (A □)・
...(Am,) group (t indicates the number) allows collection by multiple collector groups at the same time and enables switching, as well as multiple backup system collectors (A11)...(
The number of collectors in each collector group is set corresponding to the condensable gas generation lid, and continuous operation is possible without interfering with the production of ρ of the generator. In addition, inspection, repair, and periodic inspection can be carried out at any time, and malfunctions can be adequately dealt with.The condensable gas collection, discharge and recovery performance has been further improved, and reliability has been significantly improved.

さらにまた、第5図、第6図および第7図に前記各実施
例における冷却・加熱型捕集器(A、)と該捕集器(A
m)ごとに連結される冷却兼加熱ユニツ) (B、)と
の配置の具体例を示しており、冷却・加熱型捕集器(A
1)に対して冷却兼加熱ユニツ) (B、)を、側部配
置(第5図参照)、上部配置(第6図参照)、およびフ
レーム内に配置された上部配置(第7図参照)にするこ
とができる。
Furthermore, FIG. 5, FIG. 6, and FIG. 7 show the cooling/heating type collector (A,) and the collector (A,
The figure shows a specific example of the arrangement of the cooling/heating type collector (A) connected to the cooling/heating unit (A
1) cooling/heating unit) (B,) in a side arrangement (see Fig. 5), an upper arrangement (see Fig. 6), and an upper arrangement arranged in the frame (see Fig. 7). It can be done.

前記実施例における冷却兼加熱ユニットは、第2図に示
すようにコンプレッサー(C1)の吐出側に、コンデン
サー(−1)と冷媒供給弁(■3)および膨張弁(v4
)を有する冷媒発生系と、コンデンサー(−2)と熱媒
供給弁(v5)を有する熱媒発生系とを並列に連結し両
系の吐出側管路を共通にしているため、前記捕集器との
連結管路は2本となり、かつ前記捕集器ごとに連結され
ているため、冷媒と熱媒の供給機構を有しているにもか
かわらず構造が極めて簡素化されかつ著しくコンパクト
に形成でき前記のような配置が自在になっている。
The cooling/heating unit in the above embodiment includes a condenser (-1), a refrigerant supply valve (■3), and an expansion valve (v4) on the discharge side of the compressor (C1), as shown in FIG.
) and a heating medium generation system having a condenser (-2) and a heating medium supply valve (v5) are connected in parallel, and the discharge side pipe line of both systems is common. There are two pipes connected to the collector, and they are connected to each collector, so the structure is extremely simple and compact despite having a refrigerant and heat medium supply mechanism. It can be formed and arranged as described above.

(発明の効果) 前述のように本発明においては、凝結性ガスの発生装置
に連結された複数の冷却・加熱型捕集器のそれぞれに、
コンプレッサーに連結された冷媒発生系と熱媒発生系と
を有する冷却兼加熱ユニットを設けた構成になっている
ため、複数の前記捕集器の一部によって凝結性ガスを捕
集するとともに、前記捕集中に他の捕集器から捕集した
凝結性物質を払い出して回収でき、その補修点検、定期
検査さらには予冷操作も可能になって、前記操作の切換
えによって発生装置の運転を停止しないで発生される凝
結性ガスを連続的に捕集かっ払い出し回収でき、優れた
捕集、払い出し回収性能を有し信頼性が著しく向上され
ている。
(Effects of the Invention) As described above, in the present invention, each of the plurality of cooling/heating type collectors connected to the condensable gas generator has a
Since the configuration includes a cooling/heating unit having a refrigerant generation system and a heat medium generation system connected to a compressor, condensable gas is collected by some of the plurality of collectors, and the The condensable substances collected from other collectors can be discharged and collected during collection, and repair inspections, periodic inspections, and even pre-cooling operations can be performed, without having to stop the operation of the generator due to switching of the operations. The generated condensable gas can be continuously collected, discharged and recovered, and has excellent collection, discharge and recovery performance, and reliability has been significantly improved.

また、発生装置における凝結性ガスの発生量に対応させ
て前記冷却兼加熱ユニット付前記捕集器の個数を増減自
在であるとともに、前記捕集器の一部を予備系とするこ
とも可能であって、凝結性物質の捕集、払い出し回収性
能、信頼性の向上とともに、発生装置の稼働率の向上に
寄与でき発生装置の規模に対応できる汎用性を有する。
Further, the number of the collectors with cooling/heating units can be increased or decreased in accordance with the amount of condensable gas generated in the generator, and a part of the collectors can be used as a standby system. Therefore, it not only improves the performance of collecting coagulable substances, discharging and collecting them, and improves reliability, but also contributes to improving the operating rate of the generator and has the versatility to be compatible with the scale of the generator.

さらに、前記冷却兼加熱ユニットは、前記のような構成
になっておりかつ前記捕集器ごとに設けられ、しかも十
分な冷媒、熱媒の供給能力を有しているにもかかわらず
構造が著しく簡素化され大幅にコンノ(クト化されてお
り、随時に点検修理でき信頼性が高められかつ定期検査
も短時間ですむなどの利点を有するとともに、運転、据
付、撤去などが容易であるなどの特徴を有する。
Furthermore, although the cooling/heating unit has the above-mentioned configuration and is provided for each collector, and has sufficient refrigerant and heat medium supply capacity, the structure is extremely large. It has the advantages of being simplified and significantly more compact, allowing for inspection and repair at any time, increasing reliability, and requiring only a short period of time for periodic inspections, as well as ease of operation, installation, and removal. Has characteristics.

以上本発明を実施例について説明したが、勿論本発明は
このような実施例にだけ局限されるものではなく、本発
明の精神を逸脱しない範囲内で種々の設計の改変を施し
うるものである。
Although the present invention has been described above with reference to embodiments, it goes without saying that the present invention is not limited to such embodiments, and that various design modifications can be made without departing from the spirit of the present invention. .

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

第1図は本発明のM1実施例を示す凝結性物質の捕集装
置の機構図、第2図は第1図の冷却兼加熱ユニットの詳
細機構図、第3図は本発明の第2実施例を示す機構図、
第4図は本発明の第3実施例を示す機構図、第5図、M
6図および第7図は冷却・加熱型捕集器に対する冷却兼
加熱ユニットの各配置の具体例図、第8図は従来例を示
す機構図である。 N1.N2.N、 :発生装置、A111Al。1A2
11A22#A2:II’nx 1AnL a’yn、
e’mi lAA!1 eAli ”冷却・加熱型捕集
器、Bt 11Bl □zB2□5B2z+B25pB
nx *Bni sRmlm”mi eBolmBli
:冷却兼加熱ユニット、C□:コンプレッサ、g 1r
 V a 、 V 4 :冷媒発生系、’21v5”熱
媒発生系復代理人 弁理士開本重文 外2名
Fig. 1 is a mechanical diagram of a condensable substance collection device showing the M1 embodiment of the present invention, Fig. 2 is a detailed mechanical diagram of the cooling/heating unit of Fig. 1, and Fig. 3 is a second embodiment of the present invention. Mechanism diagram showing an example,
Fig. 4 is a mechanism diagram showing the third embodiment of the present invention, Fig. 5, M
6 and 7 are concrete examples of the arrangement of cooling/heating units for a cooling/heating type collector, and FIG. 8 is a mechanism diagram showing a conventional example. N1. N2. N.: Generator, A111Al. 1A2
11A22#A2:II'nx 1AnL a'yn,
e'mi lAA! 1 eAli” cooling/heating type collector, Bt 11Bl □zB2□5B2z+B25pB
nx *Bni sRmlm"mi eBolmBli
: Cooling/heating unit, C□: Compressor, g 1r
V a , V 4: Refrigerant generation system, '21v5' heating medium generation system Sub-agents: 2 patent attorneys and non-Kaimoto important academics

Claims (1)

【特許請求の範囲】[Claims] 凝結性ガスの発生装置に連結された複数の冷却・加熱型
捕集器のそれぞれに、コンプレッサーに連結された冷媒
発生系と熱媒発生系とを有する冷却兼加熱ユニットを設
けたことを特徴とする凝結性物質の捕集装置。
Each of the plurality of cooling/heating collectors connected to the condensable gas generator is provided with a cooling/heating unit having a refrigerant generation system and a heat medium generation system connected to a compressor. A collection device for coagulable substances.
JP12797285A 1985-06-14 1985-06-14 Collecting device for coagulatory material Granted JPS61287404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12797285A JPS61287404A (en) 1985-06-14 1985-06-14 Collecting device for coagulatory material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12797285A JPS61287404A (en) 1985-06-14 1985-06-14 Collecting device for coagulatory material

Publications (2)

Publication Number Publication Date
JPS61287404A true JPS61287404A (en) 1986-12-17
JPH0128601B2 JPH0128601B2 (en) 1989-06-05

Family

ID=14973244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12797285A Granted JPS61287404A (en) 1985-06-14 1985-06-14 Collecting device for coagulatory material

Country Status (1)

Country Link
JP (1) JPS61287404A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013022492A (en) * 2011-07-19 2013-02-04 Ulvac Japan Ltd Refiner

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5919503U (en) * 1982-07-27 1984-02-06 深尾精機株式会社 filling equipment

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5919503B2 (en) * 1978-02-24 1984-05-07 日本電信電話株式会社 Tracking phone method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5919503U (en) * 1982-07-27 1984-02-06 深尾精機株式会社 filling equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013022492A (en) * 2011-07-19 2013-02-04 Ulvac Japan Ltd Refiner

Also Published As

Publication number Publication date
JPH0128601B2 (en) 1989-06-05

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