JPH0271833A - Heat treatment apparatus - Google Patents
Heat treatment apparatusInfo
- Publication number
- JPH0271833A JPH0271833A JP1148189A JP14818989A JPH0271833A JP H0271833 A JPH0271833 A JP H0271833A JP 1148189 A JP1148189 A JP 1148189A JP 14818989 A JP14818989 A JP 14818989A JP H0271833 A JPH0271833 A JP H0271833A
- Authority
- JP
- Japan
- Prior art keywords
- valve
- space
- water
- discharge
- heat
- 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
- 238000010438 heat treatment Methods 0.000 title claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 89
- 239000012530 fluid Substances 0.000 claims abstract description 39
- 239000000463 material Substances 0.000 claims abstract description 5
- 150000003839 salts Chemical class 0.000 claims description 28
- 230000001105 regulatory effect Effects 0.000 claims description 10
- 238000012423 maintenance Methods 0.000 claims description 7
- 239000008400 supply water Substances 0.000 claims 1
- 239000012267 brine Substances 0.000 abstract description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract description 3
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 238000001816 cooling Methods 0.000 description 5
- 230000008901 benefit Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 108010074506 Transfer Factor Proteins 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002537 cosmetic Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/002—Component parts of these vessels not mentioned in B01J3/004, B01J3/006, B01J3/02 - B01J3/08; Measures taken in conjunction with the process to be carried out, e.g. safety measures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、熱処理用装置、特に化学工業、医薬品工業
、食品工業および化粧品工業等において使用するのに好
適な熱処理用装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a heat treatment apparatus, particularly a heat treatment apparatus suitable for use in the chemical industry, pharmaceutical industry, food industry, cosmetics industry, etc.
従来の技術
上記の工業部門において最も広く普及しているこの種の
装置は、マントルもしくは他の透熱性壁を備えた容器、
即ち、種々の化学的なプロセスや反応を分溜的に実施す
るのに適した所謂オートクレーブである。2. Prior Art The most widespread devices of this type in the industrial sectors mentioned above include vessels with mantles or other heat-permeable walls;
That is, it is a so-called autoclave suitable for carrying out various chemical processes and reactions in a fractional manner.
オートクレーブは幅広く利用できるものであるが、マン
トルまたは該装置の他のエネルギー伝導性部材へエネル
ギー媒体を移送するのに現在使用されているタイプのも
のは効率よく使用できないので、十分に冷却や加熱をお
こなうことができず、また、構造材料を確実に保護する
か、あるいは熱衝撃から装置を保護することはできない
。このため、得られる生成物の品質は適当でない場合が
多く、また、生成物の量も均一にならない。さらに、こ
の種の装置を使用するには多くの原材料、エネルギーお
よび労力を特徴とする
特に医薬品工業においては、同一のオートクレーブ内に
おいて多くの生成物が生成したり、あるいは同一の装置
内において冷却や加熱が均等におこなわれないことが多
いために、最終生成物が製造されるまでに相前後して多
くの反応が発生することが頻繁におこなわれている。従
って、オートクレーブを用いて特殊な構造を有する高価
な原料を処理する場合には多大の節約をしなければなら
ず、同時にまた、複雑な導管系と遮断制御系を必要とす
る。Although autoclaves are widely available, the types currently used to transfer the energy carrier to the mantle or other energy-conducting parts of the equipment cannot be used efficiently and must be adequately cooled and heated. It is not possible to reliably protect the structural materials or protect the equipment from thermal shock. For this reason, the quality of the product obtained is often inadequate, and the amount of product is also not uniform. Furthermore, the use of this type of equipment is characterized by a large amount of raw materials, energy and labor, especially in the pharmaceutical industry, where many products are produced in the same autoclave or cooling and Because the heating is often not uniform, many reactions frequently occur one after the other before the final product is produced. Therefore, great savings have to be made when using autoclaves to process expensive raw materials with special structures, and at the same time they also require complex conduit systems and shut-off control systems.
オートクレーブのマントルもしくは他の透熱性壁の一方
に隣接した接触面に、異なる熱媒体を保有する導管を、
2段階の閉鎖装置を介して接続させt;装置が知られて
いる。Conduits containing different heating media are placed at the contact surface adjacent to one of the autoclave mantles or other heat-permeable walls.
Devices are known which are connected via a two-stage closure device.
この既知の装置においては、熱伝導性空間内もしくはオ
ートクレーブのマントル空間内への熱媒体の流入速度は
、所定の構造を有するオートクレーブを使用する場合の
該熱媒体の輸送圧および排出手段を備えた導管の制御弁
の調節によって決定される。In this known device, the rate of inflow of the heating medium into the thermally conductive space or into the mantle space of the autoclave is determined by the transport pressure of the heating medium when using an autoclave with a certain construction and with the evacuation means. Determined by adjustment of the conduit control valve.
また、この既知の装置においては、一方では、所望の熱
伝導ファクターを達成するのに適当な熱媒体の流速を確
社できず、他方では、熱媒体の輸送量を別個に調節しな
ければならないために、非常に複雑な制御が必要となる
。さらにまた、間違った操作を避けるためには、特に複
雑な機械的および電気的閉鎖手段を必要とする。Moreover, in this known device, on the one hand, it is not possible to establish a flow rate of the heating medium suitable for achieving the desired heat transfer factor, and on the other hand, the transport rate of the heating medium has to be adjusted separately. Therefore, extremely complex control is required. Furthermore, particularly complex mechanical and electrical closure means are required to avoid incorrect operation.
オートクレーブのマントル空間への熱媒体の移動を循環
ポンプを用いておこない、該ポンプの吸引側を熱媒体用
導管調節弁を介してオートクレーブと接続させ、該調節
弁を制御することによって、循環ポンプで吸引されて該
マントル空間へ新たに輸送される熱媒体の量が決定され
る装置も知られている。The heat medium is transferred to the mantle space of the autoclave using a circulation pump, the suction side of the pump is connected to the autoclave via a heat medium conduit control valve, and the control valve is controlled. Devices are also known in which the amount of heat transfer medium that is sucked in and transported anew into the mantle space is determined.
この装置においては、新たに送給された熱媒体によって
排除された使用済の熱媒体を排出するための別個の装置
を必要とする。このような操作は一般に、熱媒体の回帰
導管に接続される圧力調節器によって確実におこなうこ
とができる。This device requires a separate device for discharging the used heat transfer medium which is displaced by the newly delivered heat transfer medium. Such an operation can generally be ensured by a pressure regulator connected to the return conduit of the heating medium.
この装置を利用することによって比較的良好な熱伝導フ
ァクターが得られるが、次の点で不利である:熱媒体用
調節弁を別個に配設しなければならず、また、熱媒体を
回帰させるためには非常に複雑な別個の圧力調節器を必
要とする。Although a relatively good heat transfer factor can be obtained by using this device, it has the following disadvantages: the heating medium control valve must be installed separately, and the heating medium must be recirculated. This requires a very complex separate pressure regulator.
この既知の装置にはさらに次の様な欠点がある:再循環
熱媒体は、熱媒体を誘導する調節弁が開放している限り
、該熱媒体を保有する外部導管の圧力下では流動しない
。調節弁が閉鎖されて系が非密状態になったときには、
熱媒体を排出させるだめに、所望により流体を導入する
ことができる。This known device also has the following disadvantage: The recirculated heat transfer medium does not flow under the pressure of the external conduit carrying it, as long as the control valve guiding the heat transfer medium is open. When the control valve is closed and the system becomes non-tight,
If desired, a fluid can be introduced in order to discharge the heating medium.
この種の循環系は前記の欠点を存するので、多目的のた
めに複数種の熱媒体を用いて作動させる装置には適して
いない。Circulating systems of this type have the above-mentioned drawbacks and are therefore not suitable for systems that operate with multiple heat carriers for multiple purposes.
発明が解決しようとする課題
この発明は、熱媒体の循環による熱供給と熱除去に関す
る利用分野を拡大し、また、化学工業、医薬品工業、食
品工業および化粧品工業における熱処理工程を、制御技
術の簡素化と効率の改善によって簡易化するためになさ
れたものである。Problems to be Solved by the Invention This invention expands the field of application related to heat supply and heat removal by circulating a heat medium, and also improves heat treatment processes in the chemical, pharmaceutical, food, and cosmetic industries by simplifying control technology. This was done to simplify the process by improving efficiency and efficiency.
この発明の課題は、作動のために流体状熱媒体を必要と
する熱処理装置の調節されI;制御器械の数を減らすと
共に、循環中に消失する流体を補充することである。The object of the invention is to reduce the number of control instruments of a heat treatment apparatus which requires a fluid heat medium for operation and to replenish the fluid lost during circulation.
課題を解決するたの手段
即ち本発明は、熱供給空間または熱供給空間が透熱性物
質を介して接合されt1内部空間を有する容器もしくは
オートクレーブ、熱媒体用空間、好ましくはマントル空
間、および循環ポンプを備えた熱媒体用導管回路を具備
する熱処理用装置におい工、熱媒体収容用空間または熱
媒体収容用空間と循環ポンプの加圧側との間に流体調節
弁が接続され、該流体調節弁の他の接続部が好ましくは
排出管に接続され、該循環ポンプの吸引側に、熱媒体導
入弁、好ましくは水導入弁および塩水導入弁を介して、
水導入管、塩水導入管またはその他の熱媒体導入管が直
接的もしくは間接的に接続されたことを特徴とする熱処
理用装置に関する。Means for solving the problem, that is, the present invention provides a heat supply space or a container or autoclave in which the heat supply spaces are joined via a heat-permeable material and has a t1 internal space, a heat medium space, preferably a mantle space, and a circulation pump. A fluid control valve is connected between the heating medium storage space or the heating medium storage space and the pressurizing side of the circulation pump, and the fluid control valve is Another connection is preferably connected to the discharge pipe and on the suction side of the circulation pump via a heat medium inlet valve, preferably a water inlet valve and a salt water inlet valve.
The present invention relates to a heat treatment apparatus characterized in that a water introduction pipe, a salt water introduction pipe, or another heat medium introduction pipe is connected directly or indirectly.
本発明による装置の好ましい実施態様においては、流体
調節弁はマントル空間の」下部に接続され、流体調節弁
が接続された側のマントル空間Iこは上部弁を介して上
部水準調節器が接続され、循環ポンプの吸引側とマント
ル空間との間には蒸気−水ミキサーと下部水準調節器が
接続され、蒸気−水ミキサーには蒸気調節弁を介して蒸
気用導管が接続され、また、循環ポンプの加圧側とマン
トル空間との間には循環弁が配設される。In a preferred embodiment of the device according to the invention, the fluid regulating valve is connected to the lower part of the mantle space, and the upper level regulator is connected via the upper valve to the mantle space I on the side to which the fluid regulating valve is connected. A steam-water mixer and a lower level regulator are connected between the suction side of the circulation pump and the mantle space, and a steam conduit is connected to the steam-water mixer via a steam control valve. A circulation valve is disposed between the pressurized side of the mantle and the mantle space.
本発明による装置の別の好ましい実施態様においては、
循環弁とマントル空間との間に凝縮水排出弁と第一排出
弁が接続され、該排出弁の他方の側は蒸気−水ミキサー
と下部水準調節器との間に接続される。この場合、循環
ポンプの加圧側と排出用導管との間に第二排出弁が接続
され、排出用導管には水排出弁と塩水排出弁が接続され
、また、水排出弁と水導入管との間には圧力維持容器と
逆止弁が配設され、圧力維持容器には好ましくは圧力調
節器が接続される。In another preferred embodiment of the device according to the invention,
A condensate discharge valve and a first discharge valve are connected between the circulation valve and the mantle space, and the other side of the discharge valve is connected between the steam-water mixer and the lower level regulator. In this case, a second discharge valve is connected between the pressurizing side of the circulation pump and the discharge conduit, a water discharge valve and a salt water discharge valve are connected to the discharge conduit, and a water discharge valve and a water inlet pipe are connected. A pressure maintenance container and a check valve are disposed between the two, and a pressure regulator is preferably connected to the pressure maintenance container.
本発明による装置のさらに別の好ましい実施態様におい
ては、水導入弁、蒸気調節弁、塩水導入弁、水排出弁、
塩水排出弁、凝縮水排出弁、上部弁、第一排出弁、循環
弁、第二排出弁、流体調節弁および循環ポンプの制御導
入口は制御装置の出口側に接続され、また、下部水準調
節器、上部水準調節器および圧力調節用排出口は制御装
置の入口側に接続される。In a further preferred embodiment of the device according to the invention, a water inlet valve, a steam regulating valve, a brine inlet valve, a water outlet valve,
The salt water discharge valve, condensate discharge valve, upper valve, first discharge valve, circulation valve, second discharge valve, fluid control valve and circulation pump control inlet are connected to the outlet side of the control device, and the lower level control is connected to the outlet side of the control device. The upper level regulator and pressure regulating outlet are connected to the inlet side of the control device.
本発明による装置とその機能を第1図に基づいてさらに
詳述する。The device according to the invention and its function will be explained in more detail on the basis of FIG.
第1図は本発明による装置の一実施態様を示す回路図で
ある。FIG. 1 is a circuit diagram showing one embodiment of a device according to the invention.
第1図に示す本発明による装置は外部マントル(22)
と内部マントル(21)を有する自体既知のオートクレ
ーブ(19)を具備し、該オートクレーブの内部空間に
はミギサー(20)が配設される。The device according to the invention shown in FIG.
The autoclave is equipped with an autoclave (19) known per se, having an internal mantle (21) and an internal space of the autoclave in which a mixer (20) is disposed.
オートクレーブ(19)の外部マン[・ル(22)と内
部マントル(21)との間には、マントル空間(23)
か形成される。マントル空間(23)の下部には、循環
弁(9)を介して、循環ポンプ(15)の加圧側か接続
され、該マントル空間の一方の側部の上部には蒸気−水
ミキサー(14)、導入管(30)および下部水準調節
器(12)を介して、循環ポンプ(15)の吸引側が接
続される。導入管(3o)には、水導入弁(1)、圧力
維持容器(16)および逆止弁(18)を介して、水導
入管(27)が接続されると共に、塩水導入弁(3)を
介して塩水導入管(28)が接続される。圧力維持容器
(16)には圧力調節器(17)が接続される。There is a mantle space (23) between the outer mantle (22) and the inner mantle (21) of the autoclave (19).
or formed. The pressurizing side of a circulation pump (15) is connected to the lower part of the mantle space (23) via a circulation valve (9), and a steam-water mixer (14) is connected to the upper part of one side of the mantle space. , the suction side of the circulation pump (15) is connected via the inlet pipe (30) and the lower level regulator (12). A water introduction pipe (27) is connected to the introduction pipe (3o) via a water introduction valve (1), a pressure maintenance container (16), and a check valve (18), and a salt water introduction valve (3) A salt water inlet pipe (28) is connected via the salt water inlet pipe (28). A pressure regulator (17) is connected to the pressure maintenance container (16).
循環弁(9)とマントル空間(23)の間には第一排出
弁(8)の一方の側が接続され、該排出弁(8)の他方
の側は導入管(30)に接続される。循環ポンプ(15
)の加圧側は第二排出弁(10)を介して排出管(26
)に接続され、該排出管には水排出弁(4)と塩水排出
弁(5)が連結される。循環弁(9)とマントル空間(
23)の間には凝縮水排出弁(6)が接続される。One side of a first discharge valve (8) is connected between the circulation valve (9) and the mantle space (23), and the other side of the first discharge valve (8) is connected to the introduction pipe (30). Circulation pump (15
) is connected to the discharge pipe (26) via the second discharge valve (10).
), and a water discharge valve (4) and a salt water discharge valve (5) are connected to the discharge pipe. Circulation valve (9) and mantle space (
23) is connected with a condensed water discharge valve (6).
マントル空間(23)の他方の側部には上部弁(7)を
介して上部水準調節器(13)が接続され、マントル空
間(23)と排出管(26)との間には流体調節弁(1
1)が配設される。蒸気−水ミキサー(14)には蒸気
調節弁(2)を介して蒸気管(l l)が接続される。An upper level regulator (13) is connected to the other side of the mantle space (23) via an upper valve (7), and a fluid control valve is connected between the mantle space (23) and the discharge pipe (26). (1
1) is provided. A steam pipe (ll) is connected to the steam-water mixer (14) via a steam control valve (2).
水導入弁(1)、蒸気調節弁(2)、塩水導入弁(3)
、水排出弁(4)、塩水排出弁(5)、凝縮水排出弁(
6)、上部弁(7)、第一排出弁(8)、循環弁(9)
、第二排出弁(lO)、流体調節弁(11)および循環
ポンプ(15)の制御導入口は制御装置(25)の出口
側に接続され、一方、下部水準調節器(12)、上部水
準調節器(13)および圧力調節器(17)の排出口は
制御装置(25)の入口側に接続される。Water introduction valve (1), steam control valve (2), salt water introduction valve (3)
, water discharge valve (4), salt water discharge valve (5), condensed water discharge valve (
6), upper valve (7), first discharge valve (8), circulation valve (9)
, the second discharge valve (lO), the fluid regulating valve (11) and the control inlets of the circulation pump (15) are connected to the outlet side of the control device (25), while the lower level regulator (12), the upper level The outlets of the regulator (13) and the pressure regulator (17) are connected to the inlet side of the control device (25).
第1図に示す本発明による装置の操作は次の様にしてお
こなわれる。The operation of the device according to the invention shown in FIG. 1 is carried out as follows.
冷却流体を用いて操作する場合には、第一排出弁(8)
、凝縮水排出弁(6)、第二排出弁(40)および流体
調節弁(11)を閉鎖状態にし、水導入弁(1)もしく
は塩水導入弁(3)を開放することによって空の系内へ
水もしくは塩水を導入する。この流体導入は、上部水準
調節器(13)が、制御装置(25)の充填状態を示す
までおこなわれる。次いで、上部弁(7)を制御装置(
25)によって閉鎖した後、循環ポンプ(15)を作動
させる。When operating with cooling fluid, the first discharge valve (8)
, by closing the condensed water discharge valve (6), the second discharge valve (40), and the fluid control valve (11), and opening the water introduction valve (1) or the salt water introduction valve (3). Introduce water or salt water to the tank. This fluid introduction takes place until the upper level regulator (13) indicates the filling status of the control device (25). Then, the upper valve (7) is connected to the control device (
After closing by 25), the circulation pump (15) is activated.
循環に際しては、調整された温度値に対応して、制御装
置(25)によって流体調節弁(11)を開放するが、
この場合、塩水もしくは水の循環路から奪われる熱量に
よってオートクレーブ(19)の内部(24)の温度が
所定の値に維持されるように該流体調節弁を調節する。During circulation, the control device (25) opens the fluid control valve (11) in response to the adjusted temperature value.
In this case, the fluid control valve is adjusted so that the temperature inside (24) of the autoclave (19) is maintained at a predetermined value by the amount of heat removed from the salt water or water circulation path.
熱媒体として使用される流体は任意の技術的に適当な流
体、例えば石油等であってもよい。The fluid used as heat transfer medium may be any technically suitable fluid, such as petroleum or the like.
循環中は対応する手段、例えば水もしくは塩水を導入さ
せる水導入弁(1)もしくは塩水導入弁(3)を全開さ
せ、流出する熱媒体は対応する導管、例えは水導入管(
27)もしくは塩水導入管(28)から直ちに補充する
。During circulation, the corresponding means, for example the water inlet valve (1) or the salt water inlet valve (3) for introducing water or salt water, are fully opened, and the outflowing heat medium is passed through the corresponding conduit, for example the water inlet pipe (
27) or immediately refill from the salt water inlet pipe (28).
循環する流体からは、流体調節弁(11)の状態と補充
される流体状熱媒体の圧力比に応じた量に対応して、使
用済の流体は流体調節弁(11)あるいは排出管(26
)または水排出弁(4)もしくは塩水排出弁(5)を介
して排出される。From the circulating fluid, used fluid is removed from the fluid control valve (11) or the discharge pipe (26) depending on the state of the fluid control valve (11) and the pressure ratio of the fluid heat medium to be replenished.
) or via the water discharge valve (4) or the salt water discharge valve (5).
塩水排出弁(5)によって塩水を排出させた後、塩水冷
却工程を切り換えることができる。この切り換えは、循
環ポンプ(15)の作用により、第一排出弁(8)と第
二排出弁(11)を介して系を完全に空にすることによ
って容易におこなわれる。After draining the salt water by means of the salt water discharge valve (5), the salt water cooling process can be switched. This changeover is easily carried out by completely emptying the system via the first drain valve (8) and the second drain valve (11) by the action of the circulation pump (15).
系が空の状態にあることが制御装置(25)の下部水準
調節器(12)によって表示された後で一次の工程、例
えば水冷却工程の開始指令が与えられる。After the empty state of the system has been indicated by the lower level regulator (12) of the control device (25), the command to start the primary process, for example the water cooling process, is given.
水冷却工程を温熱水加熱工程に切り換える場合には、制
御装置(25)の制御下において、蒸気調節弁(2)の
開放状態に対応する量の蒸気が蒸気−水ミキサー(14
)内で凝縮し、該凝縮水は循環水と混合する。When switching the water cooling process to the hot water heating process, under the control of the control device (25), an amount of steam corresponding to the open state of the steam control valve (2) is transferred to the steam-water mixer (14).
), and the condensed water mixes with the circulating water.
蒸気−水ミキサー(14)内での蒸気の凝縮によって得
られる水の量は循環水の量を増加させる。これを避ける
ためには、過剰量の水を圧力容器内にトラップし、該容
器内における過度の圧力上昇は圧力調節器(17)によ
って防止される。該圧力調節弁は、制御装置(25)が
調節された圧力値に達すると、上部弁(7)を開放すべ
き指令を与えるので、過剰水は上部水準調節器(13)
を介して排出管へ流出させる。水導入管(27)内への
凝縮水の流入は逆止弁(18)によって防止される。こ
の系は温熱水加熱工程の場合も、水導入管(27)の圧
力下にある。The amount of water obtained by condensing the steam in the steam-water mixer (14) increases the amount of circulating water. To avoid this, excess water is trapped in a pressure vessel, in which excessive pressure build-up is prevented by a pressure regulator (17). The pressure regulating valve gives a command to open the upper valve (7) when the control device (25) reaches the regulated pressure value, so that the excess water flows through the upper level regulator (13).
through the drain pipe. A check valve (18) prevents condensed water from flowing into the water introduction pipe (27). This system is also under pressure in the water inlet pipe (27) during the hot water heating process.
蒸気加熱工程の場合には、蒸気導管(29)からの蒸気
は調節弁(2)を通ってオートクレーブのマントル空間
(23)内に流入して凝縮するので、循環ポンプは作動
させない。マントル空間(23)に接続された凝縮水排
出用弁(6)の機能によって、凝縮水は確実に排出され
る。In the case of a steam heating process, the steam from the steam conduit (29) flows through the regulating valve (2) into the mantle space (23) of the autoclave and condenses, so that the circulation pump is not activated. The condensed water is reliably discharged by the function of the condensed water discharge valve (6) connected to the mantle space (23).
上述の実施態様から明らかなように、熱媒体として任意
の流体を使用する場合、循環系内へ導入する流体量およ
び該系外へ排出する流体量は流体調節弁(11)の操作
のみによって規定することができ、また、該調節弁によ
って導管内の圧力を一定に調整できる。また、任意の流
体状熱媒体を使用する場合、対応する放熱量と吸熱量の
変動も流体調節弁(11)によって調整できる。As is clear from the embodiments described above, when using any fluid as a heat medium, the amount of fluid introduced into the circulation system and the amount of fluid discharged from the system can be determined only by the operation of the fluid control valve (11). In addition, the pressure in the conduit can be constantly adjusted by the regulating valve. Further, when using any fluid heat medium, the corresponding fluctuations in the amount of heat released and absorbed can be adjusted by the fluid control valve (11).
熱媒体を導入する場合にはさらに2段階弁、例えば水導
入弁(1)または塩水導入弁(3)のみを必要とするだ
けである。何故ならば、これらの調整は流体調節弁(1
1)の作動を調整することによって確実におこなうこと
ができるからである。In the case of introducing a heating medium, only a two-stage valve, for example a water inlet valve (1) or a salt water inlet valve (3), is required. This is because these adjustments are made using the fluid control valve (1
This is because it can be performed reliably by adjusting the operation of 1).
発明の効果
本発明による装置の利点は、既知のこの種の装置に比較
して、制御エレメントの数が少ないので、調整か実質上
より簡単化されるだけでなく、任意の流体状熱媒体が使
用できるので実用的であることである。Effects of the Invention The advantage of the device according to the invention is that, compared to known devices of this kind, it not only has a smaller number of control elements, which makes the regulation substantially easier, but also that any fluid heat carrier can be used. It is practical because it can be used.
本発明による装置の別の利点は、冷却から加熱へ切り換
える際の移行が実際上完全に連続的におこなわれるので
、過渡温度(Temperaturtransient
e)の低下もしくは回避が可能となり、また、オートク
レーブ内で処理された物質は熱衝撃を受けないことであ
る。Another advantage of the device according to the invention is that the transition when switching from cooling to heating takes place virtually completely continuously, so that no temperature transients are detected.
e) can be reduced or avoided, and the material treated in the autoclave is not subjected to thermal shock.
本発明によるさらに別の利点は、温度変化が連続的にお
こなわれるので、過度に急激で、損傷をもたらすことの
ある温度の作用からオートクレーブが適切に保護される
ことである。A further advantage of the invention is that, since the temperature changes are continuous, the autoclave is adequately protected from excessively rapid and potentially damaging temperature effects.
第1図は本発明による装置の一実施態様を示す回路図で
ある。
(1)は水導入弁、(2)は蒸気調節弁、(3)は塩水
導入弁、(4)は水排出弁、(5)は塩水排出弁、(6
)は凝縮水排出弁、(7)は上部弁、(8)は第一排出
弁、(9)は循環弁、(l O)は第二排出弁、(11
)は流体調節弁、(12)は下部水準調節器、(13)
は上部水準調節器、(14)は蒸気−水ミキサ、(15
)は循環ポンプ、(16)は圧力維持容器、(17)は
圧力調節器、(18)は逆止弁、(19)はオートクレ
ーブ、(20)はミキサー、(21)は内部マントノ呟
(22)は外部マントル、(23)はマントル空間、(
24)はオートクレーブ内部、(25)は制御装置、(
26)は排出管、(27)は水導入管、(28)は塩水
導入管、(29)蒸気導入管、(30)は導入管を示す
。
特許出願人 キノイン・ヂョーヂイセル・ニーシュ・ヴ
エヂエーセチ・テルメーケク・FIG. 1 is a circuit diagram showing one embodiment of a device according to the invention. (1) is water inlet valve, (2) is steam control valve, (3) is salt water inlet valve, (4) is water discharge valve, (5) is salt water discharge valve, (6
) is the condensed water discharge valve, (7) is the upper valve, (8) is the first discharge valve, (9) is the circulation valve, (l O) is the second discharge valve, (11
) is the fluid control valve, (12) is the lower level regulator, (13)
is the upper level controller, (14) is the steam-water mixer, (15
) is the circulation pump, (16) is the pressure maintenance vessel, (17) is the pressure regulator, (18) is the check valve, (19) is the autoclave, (20) is the mixer, (21) is the internal mantle (22) ) is the external mantle, (23) is the mantle space, (
24) is inside the autoclave, (25) is the control device, (
26) is a discharge pipe, (27) is a water introduction pipe, (28) is a salt water introduction pipe, (29) is a steam introduction pipe, and (30) is an introduction pipe. Patent applicant
Claims (1)
接合された内部空間を有する容器もしくはオートクレー
ブ、熱媒体用空間、好ましくはマントル空間、および循
環ポンプを備えた熱媒体用導管回路を具備する熱処理用
装置において、熱媒体収容用空間または熱媒体収容用空
間と循環ポンプ(15)の加圧側との間に流体調節弁(
11)が接続され、 該流体調節弁の他の接続部が好ましくは排出管(26)
に接続され、 該循環ポンプの吸引側に、熱媒体導入弁、好ましくは水
導入弁(1)および塩水導入弁(3)を介して、水導入
管(27)、塩水導入管(28)またはその他の熱媒体
導入管が直接的もしくは間接的に接続されたことを特徴
とする熱処理用装置。 2、流体調節弁(11)がマントル空間(23)の上部
に接続され、流体調節弁(11)のマントル空間(23
)に接続した側に上部弁(7)を介して上部水準調節器
(13)が接続され、循環ポンプ(15)の吸引側とマ
ントル空間(23)との間に蒸気−水ミキサー(14)
と下部水準調節器(12)が接続され、蒸気−水ミキサ
ー(14)に蒸気調節弁(2)を会して蒸気導管(29
)が接続され、循環ポンプ(15)の加圧側とマントル
空間(23)との間に循環弁(9)が配設された請求項
1記載の熱処理用装置。 3、循環弁(9)とマントル空間(23)との間に凝縮
水排出弁(6)と第一排出弁(8)が接続され、該第一
排出弁の他方の側が蒸気−水ミキサー(14)と下部水
準調節器(12)に接続され、循環ポンプ(15)の加
圧側と排出管(26)との間に第二排出弁(10)が接
続され、排出管(26)に水排出弁(4)と塩水排出弁
(5)が接続され、水導入弁(1)と水導入管(27)
の間に圧力維持容器(16)と逆止弁(18)が配設さ
れ、圧力維持容器(16)に好ましくは圧力調節器(1
7)が接続された請求項1もしくは2記載の熱処理装置
。 4、水導入弁(1)、蒸気調節弁(2)、塩水導入弁(
3)、水排出弁(4)、塩水排出弁(5)、凝縮水排出
弁(6)、上部弁(7)、第一排出弁(8)、循環弁(
9)、第二排出弁(10)、流体調節弁(11)および
循環ポンプ(15)の制御導入口が制御装置(25)の
出口側に接続され、下部水準調節器(12)、上部水準
調節器(13)および圧力調節器(17)の出口が制御
装置(25)に接続された請求項1〜3いずれかに記載
の熱処理装置。[Claims] 1. A container or autoclave having a heat supply space or an internal space to which the heat supply space is connected via a heat-permeable material, a heat medium space, preferably a mantle space, and a heat source equipped with a circulation pump. In a heat treatment apparatus equipped with a medium conduit circuit, a fluid control valve (
11) is connected, and the other connection of the fluid regulating valve is preferably a discharge pipe (26).
A water inlet pipe (27), a salt water inlet pipe (28) or A heat treatment device characterized in that another heat medium introduction pipe is connected directly or indirectly. 2. The fluid control valve (11) is connected to the upper part of the mantle space (23), and the fluid control valve (11) is connected to the mantle space (23).
) is connected to the upper level regulator (13) via the upper valve (7), and a steam-water mixer (14) is connected between the suction side of the circulation pump (15) and the mantle space (23).
A lower level regulator (12) is connected to the steam-water mixer (14) and a steam control valve (2) is connected to the steam conduit (29).
) is connected thereto, and a circulation valve (9) is disposed between the pressurizing side of the circulation pump (15) and the mantle space (23). 3. A condensate discharge valve (6) and a first discharge valve (8) are connected between the circulation valve (9) and the mantle space (23), and the other side of the first discharge valve is connected to a steam-water mixer ( 14) and the lower level regulator (12), and a second discharge valve (10) is connected between the pressurizing side of the circulation pump (15) and the discharge pipe (26), and a second discharge valve (10) is connected to the discharge pipe (26) to supply water to the discharge pipe (26). The discharge valve (4) and the salt water discharge valve (5) are connected, and the water inlet valve (1) and the water inlet pipe (27)
A pressure maintenance container (16) and a check valve (18) are disposed between the pressure maintenance container (16) and a pressure regulator (1).
7) is connected to the heat treatment apparatus according to claim 1 or 2. 4. Water introduction valve (1), steam control valve (2), salt water introduction valve (
3), water discharge valve (4), salt water discharge valve (5), condensed water discharge valve (6), upper valve (7), first discharge valve (8), circulation valve (
9), the second discharge valve (10), the fluid control valve (11) and the control inlet of the circulation pump (15) are connected to the outlet side of the control device (25), the lower level regulator (12), the upper level The heat treatment apparatus according to any one of claims 1 to 3, wherein the outlets of the regulator (13) and the pressure regulator (17) are connected to a control device (25).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HU2972/88 | 1988-06-08 | ||
HU882972A HU210018B (en) | 1988-06-08 | 1988-06-08 | Equipment for chemical reactors |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0271833A true JPH0271833A (en) | 1990-03-12 |
Family
ID=10961947
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1148189A Pending JPH0271833A (en) | 1988-06-08 | 1989-06-08 | Heat treatment apparatus |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPH0271833A (en) |
BR (1) | BR8902676A (en) |
CH (1) | CH679128A5 (en) |
DE (1) | DE3915915C2 (en) |
FR (1) | FR2632718B1 (en) |
HU (1) | HU210018B (en) |
IT (1) | IT1230861B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0499228U (en) * | 1991-01-14 | 1992-08-27 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2732128B1 (en) * | 1995-03-24 | 1997-07-11 | Toulouse Inst Nat Polytech | METHOD FOR THERMAL CONTROL OF A VERSATILE DISCONTINUOUS REACTOR FROM A PLURALITY OF THERMAL FLUID SOURCES, AND DEVICE FOR CARRYING OUT SAID METHOD |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2788264A (en) * | 1953-05-25 | 1957-04-09 | Shell Dev | Apparatus for temperature control of chemical reaction vessels |
GB1322701A (en) * | 1969-04-01 | 1973-07-11 | Waddleton N | Apparatus for converting liquid fatty nitriles to amines |
CA994050A (en) * | 1971-05-12 | 1976-07-27 | Francis Sisti | Method for controlling the reaction rate of polymerization reactions |
DE2504659C3 (en) * | 1975-02-05 | 1988-02-11 | Hüls AG, 4370 Marl | Process for the controlled removal of reaction heat in polymerization reactions in dispersion or solution |
DE3102791A1 (en) * | 1981-01-28 | 1982-08-26 | Waste-Heizungen GmbH, 3012 Langenhagen | Method for regulating the thermal economy of a heat consumer or heat generator and apparatus for carrying out the method |
JPS60248702A (en) * | 1984-05-24 | 1985-12-09 | Mitsubishi Rayon Co Ltd | Method and device to control polymerization reaction |
-
1988
- 1988-06-08 HU HU882972A patent/HU210018B/en unknown
-
1989
- 1989-05-16 DE DE3915915A patent/DE3915915C2/en not_active Expired - Fee Related
- 1989-05-22 CH CH1913/89A patent/CH679128A5/de not_active IP Right Cessation
- 1989-06-06 IT IT8920790A patent/IT1230861B/en active
- 1989-06-07 FR FR8907529A patent/FR2632718B1/en not_active Expired - Fee Related
- 1989-06-07 BR BR898902676A patent/BR8902676A/en active Search and Examination
- 1989-06-08 JP JP1148189A patent/JPH0271833A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0499228U (en) * | 1991-01-14 | 1992-08-27 |
Also Published As
Publication number | Publication date |
---|---|
CH679128A5 (en) | 1991-12-31 |
IT8920790A0 (en) | 1989-06-06 |
HU210018B (en) | 1995-01-30 |
HUT50063A (en) | 1989-12-28 |
FR2632718B1 (en) | 1994-02-04 |
BR8902676A (en) | 1990-01-23 |
DE3915915A1 (en) | 1989-12-14 |
IT1230861B (en) | 1991-11-08 |
FR2632718A1 (en) | 1989-12-15 |
DE3915915C2 (en) | 1994-11-10 |
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