JPS6064108A - Decompression steam heater - Google Patents
Decompression steam heaterInfo
- Publication number
- JPS6064108A JPS6064108A JP17162383A JP17162383A JPS6064108A JP S6064108 A JPS6064108 A JP S6064108A JP 17162383 A JP17162383 A JP 17162383A JP 17162383 A JP17162383 A JP 17162383A JP S6064108 A JPS6064108 A JP S6064108A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- steam
- reducing valve
- secondary side
- reduced pressure
- 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
Links
- 230000006837 decompression Effects 0.000 title description 3
- 238000010438 heat treatment Methods 0.000 claims description 27
- 238000010586 diagram Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Devices For Use In Laboratory Experiments (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は、小型軽量にして安価な装置で常時安定した減
圧スチームを供給することにより、被処理物を通常10
0°C以下の温度で安全且つ効率的に加熱処理すること
ができる減圧スチーム加熱装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention uses a small, lightweight, and inexpensive device to constantly supply stable reduced pressure steam, thereby reducing the
The present invention relates to a reduced pressure steam heating device that can perform heat treatment safely and efficiently at temperatures below 0°C.
各種製造工場等においては、加熱処理が広く行なわれて
いる。一般に、かかる加熱処理は、被加熱物を100°
C以上の比較的高温で加熱することが多く、ボイラから
のスチームを単純利用した、全体として加圧系の加熱装
置を用いて行なっている〇
一方、化学工場等においては、作業の安全や製品の品質
の関係で、被加熱物を100°C以下の比較的低温で加
熱しなければならない場合がある。Heat treatment is widely performed in various manufacturing plants. Generally, such heat treatment involves heating the object at 100°
Heating is often done at a relatively high temperature of C or higher, and is carried out using pressurized heating equipment that simply uses steam from the boiler.On the other hand, in chemical factories, etc., there are concerns about work safety. There are cases where the object to be heated must be heated at a relatively low temperature of 100° C. or less due to product quality.
このような場合に従来、前記したような加圧系の加熱装
置を応用して、高価な圧力制御機構(PIC)や温度制
御機構(TIC)を駆使し、実際には相当量のスチーム
ロスを甘受しつつ、減圧スチームを発生させて加熱する
ことや、温水で加熱することが行なわれている。In such cases, conventionally, a pressurized heating device such as the one described above has been applied, and an expensive pressure control mechanism (PIC) and temperature control mechanism (TIC) have been used to effectively reduce a considerable amount of steam loss. Some people have been reluctant to heat it by generating reduced pressure steam or heating it with hot water.
しかし、PICやTICを駆使すればそれだけ高価にな
り、相当量のスチームロスを甘受すれば熱エネルギの面
で非効率的になることは避けられない。また、温水は熱
容量が小さく、境膜伝熱係数も低いため加熱効率が悪く
、必然に加熱装置も大型で重量に富むようになる。However, the more PIC or TIC is used, the more expensive it becomes, and if a considerable amount of steam loss is accepted, it will inevitably become inefficient in terms of heat energy. In addition, hot water has a small heat capacity and a low film heat transfer coefficient, so heating efficiency is poor, and the heating device is inevitably large and heavy.
本発明は、斜上の如き実情に鑑み、従来欠点を解消する
改良された減圧スチーム加熱装置を提供するものである
。The present invention takes into consideration the actual situation of sloping heating, and provides an improved reduced pressure steam heating device that eliminates the conventional drawbacks.
以下、図面に基づいて本発明の構成を詳細に説明する。Hereinafter, the configuration of the present invention will be explained in detail based on the drawings.
第1図は本発明の一実施例を示す系統図、第2図は本発
明における減圧弁を例示する略視図である。間接加熱容
器1に減圧弁2とスチームトラップ3とが接続されてい
る。減圧弁2の一次側Plに図中矢印Aの如く供給され
たスチームを、スチームトラップ3の二次側S2に接続
されている減圧ポンプ4で誘導し、減圧弁2の二次側P
2及び間接加熱容器1並びにスチームドラッグ30間に
減圧系を形成させ、間接加熱容器1を減圧スチームで加
熱する構成である。FIG. 1 is a system diagram showing one embodiment of the present invention, and FIG. 2 is a schematic diagram illustrating a pressure reducing valve in the present invention. A pressure reducing valve 2 and a steam trap 3 are connected to the indirect heating container 1. The steam supplied to the primary side Pl of the pressure reducing valve 2 as shown by the arrow A in the figure is guided by the pressure reducing pump 4 connected to the secondary side S2 of the steam trap 3,
2, the indirect heating container 1, and the steam drag 30, a reduced pressure system is formed between the indirect heating container 1 and the steam drag 30, and the indirect heating container 1 is heated with reduced pressure steam.
本発明において、減圧弁2は、その二次側の減圧程度に
より作動する逆負荷をかけられた弁5を有している。す
なわち、上下動用能な同県6を備える圧力室7に、弁5
と連結の画壁8が取シ付けられており、該画壁8には負
荷9が図面の場合下方へかけられている。二次側P2の
減圧程度が所望値よりも絶対圧で低い場合(系を減圧に
しすぎた場合)、該減圧程度が負荷9に打ち勝って、弁
5を図中上方へ移動させ、したがってそれだけ多くのス
チームが一次側P+から二次側P2へと通過するため、
二次側P2の減圧程度が絶対圧で高くなり、系の減圧程
度が所望値に調整される。逆に、二次側P2の減圧程度
が所望値よシも絶対圧で高い場合(系をよシ減圧にする
必要のある場合)、該減圧程度が負荷9に打ち負けて、
負荷9が弁5を図中下方へ移動させ、したがってそれだ
け少ないスチームだけしか一次側P1から二次側P2へ
と通過しないため、二次側P2の減圧程度が絶対圧で低
くなシ、系の減圧程度が所望値に調整される。In the present invention, the pressure reducing valve 2 has a reversely loaded valve 5 that operates depending on the degree of pressure reduction on its secondary side. That is, a valve 5 is installed in a pressure chamber 7 equipped with a valve 6 capable of vertical movement.
A connecting wall 8 is attached to the wall 8, and a load 9 is applied downward in the drawing. If the degree of pressure reduction on the secondary side P2 is lower in absolute pressure than the desired value (if the system is depressurized too much), the degree of pressure reduction will overcome the load 9 and move the valve 5 upward in the figure, thus increasing the Since the steam passes from the primary side P+ to the secondary side P2,
The degree of pressure reduction on the secondary side P2 increases in absolute pressure, and the degree of pressure reduction in the system is adjusted to a desired value. On the other hand, if the degree of pressure reduction on the secondary side P2 is higher in absolute pressure than the desired value (when it is necessary to further reduce the pressure in the system), the degree of pressure reduction overcomes the load 9,
The load 9 moves the valve 5 downward in the figure, and therefore only a small amount of steam passes from the primary side P1 to the secondary side P2, so the degree of pressure reduction on the secondary side P2 is low in absolute pressure, and the system The degree of pressure reduction is adjusted to a desired value.
従来のように、本来加圧系で使用される減圧弁は、第3
図の如き場合において、例えば画壁8aが基壁10に対
しスプリング11で支持され、該画壁8aにはスプリン
グ11の押圧力で図中上方に負荷がかかっている。した
がって、その作用の一例を挙げると、二次側P2の圧力
が所望値よシも低い場合(系の圧力が足らない場合)、
該圧力がスプリング11の押圧力に打ち負けて、スプリ
ング11の押圧力が弁5aを上方へ移動させ、この結果
それだけ多くのスチームが一次側P1から二次側P2へ
と通過するため、二次側の圧力が高くなり、系の圧力が
所望値に調整されるという構成であるが、二次側P2の
圧力が大気圧以下の場合は、作動しない。Conventionally, the pressure reducing valve originally used in the pressurized system is
In the case shown in the figure, for example, a drawing wall 8a is supported by a spring 11 against a base wall 10, and a load is applied to the drawing wall 8a upward in the drawing due to the pressing force of the spring 11. Therefore, to give an example of its effect, when the pressure on the secondary side P2 is lower than the desired value (when the system pressure is insufficient),
This pressure is overcome by the pressing force of the spring 11, and the pressing force of the spring 11 moves the valve 5a upward, and as a result, as much steam passes from the primary side P1 to the secondary side P2, the secondary Although the pressure on the secondary side increases and the system pressure is adjusted to a desired value, it does not operate if the pressure on the secondary side P2 is below atmospheric pressure.
要するに、本発明における減圧弁は、系の減圧状態(絶
対圧で大気圧よシ低い圧力状態)を制御するため、第3
図の如き従来の減圧弁とは作用機構が全く逆になってお
り、その二次側の減圧程度により作動する逆負荷をかけ
られた弁を有しているのである。In short, the pressure reducing valve in the present invention controls the pressure reduction state of the system (absolute pressure, which is lower than atmospheric pressure).
The operating mechanism is completely opposite to that of the conventional pressure reducing valve as shown in the figure, and the valve has a reverse load that operates depending on the degree of pressure reduction on the secondary side.
また本発明において、スチームトラップ3は、その−次
側S1から二次側S2に絶えず連通ずるバイパスを備え
ている。従来のように、本来加圧系で使用されるスチー
ムトラップにも、バイパスが設けられている。しかし、
かかる従来品のバイパスは、スチームの通過開始時やト
ラップされるスチーム量等によシ、その−次側と二次側
とを断続して連通ずるものである。この種の従来品によ
ると、本発明のように、スチームトラップ3の二次側S
2に接続されている減圧ポンプ4でスチームを誘導して
系の減圧状態等を制御する場合、その安定制御が著るし
く困難である。すなわち、本発明のごとき系の減圧制御
等をする場合、従来のスチームトラップを使用すると所
謂脈動が発生し、これが系の減圧制御等に著るしい障害
となるのである。Further, in the present invention, the steam trap 3 is provided with a bypass that constantly communicates from the downstream side S1 to the secondary side S2. Conventionally, a steam trap originally used in a pressurized system is also provided with a bypass. but,
Such a conventional bypass connects the downstream side and the secondary side intermittently depending on the start of passage of steam, the amount of trapped steam, etc. According to this type of conventional product, as in the present invention, the secondary side S of the steam trap 3
When controlling the depressurized state of the system by guiding steam using the decompression pump 4 connected to the decompression pump 2, stable control is extremely difficult. That is, when controlling the pressure reduction of a system such as the one of the present invention, if a conventional steam trap is used, so-called pulsation occurs, which becomes a serious obstacle to the pressure reduction control of the system.
本発明において、系の減圧制御等を確実に行ない、した
がって間接加熱容器1に安定して減圧スチームを供給す
るには、前述の如く、系の減圧制御等に好適改良された
減圧弁及びスチームトラップを組み込むことが肝要なの
である。In the present invention, in order to reliably control system pressure reduction, etc., and therefore stably supply reduced pressure steam to the indirect heating vessel 1, as described above, a pressure reducing valve and a steam trap that are suitably improved for system pressure reduction control, etc. are required. It is important to incorporate.
次の第1表は、第1図に例示したような本発明に係る減
圧スチーム加熱装置を用いて減圧スチームを発生させ、
該減圧スチームの通過ジャケントを備える間接加熱容器
に22℃の水を連続流入させた場合の試験結果の一例で
ある。この第1表より、減圧弁の二次側の温度及び圧力
は、負荷(水の流量)の変動にかかわらず、一定に近い
値を示していることが判る。The following Table 1 shows the results of generating reduced pressure steam using the reduced pressure steam heating device according to the present invention as illustrated in FIG.
This is an example of test results when water at 22° C. was continuously flowed into an indirect heating container equipped with a jacket through which the reduced pressure steam passed. From Table 1, it can be seen that the temperature and pressure on the secondary side of the pressure reducing valve exhibit nearly constant values regardless of fluctuations in the load (water flow rate).
第1表
(*1:絶対圧)
以上説明した本発明によると、小型軽量にして安価な装
置で常時安定した減圧スチームを供給することができ、
しだがって被処理物を通常100℃以下の比較的低温で
安全且つ効率的に加熱処理することができる効果がある
。Table 1 (*1: Absolute pressure) According to the present invention described above, it is possible to constantly supply stable reduced pressure steam with a small, lightweight, and inexpensive device.
Therefore, there is an effect that the object to be treated can be safely and efficiently heat-treated at a relatively low temperature, usually 100° C. or lower.
第1図は本発明の一実施例を示す系統図、第2図は本発
明における減圧弁を例示する略視図、第3図は従来の減
圧弁を例示する略視図である。
■・間接加熱容器、2・・・減圧弁、
3−・・スチームトラップ、4・・・減圧ポンプ、5.
5a・・弁、6.6a・周壁、 7.7a・・圧力室、
8.8a・・・画壁、9・・・負荷、10・・・基壁、
11・・・スプリング、
特許出願人 中央化工機株式会社
代理人 弁理士 入 山 宏 正
第1図
第2図
第3図FIG. 1 is a system diagram showing an embodiment of the present invention, FIG. 2 is a schematic diagram illustrating a pressure reducing valve according to the present invention, and FIG. 3 is a schematic diagram illustrating a conventional pressure reducing valve. ■・Indirect heating container, 2...pressure reducing valve, 3-...steam trap, 4...pressure reducing pump, 5.
5a...valve, 6.6a...peripheral wall, 7.7a...pressure chamber,
8.8a...Painting wall, 9...Load, 10...Base wall,
11...Spring, Patent Applicant Chuo Kakoki Co., Ltd. Agent Patent Attorney Hiroshi Iriyama Figure 1 Figure 2 Figure 3
Claims (1)
とが接続され、減圧弁の一次側に供給されたスチームを
スチームトラップの二次側に接続された減圧ポンプで誘
導することにより、減圧弁の二次側及び間接加熱容器並
びにスチームトラップの間に所望の減圧系を形成させ、
間接加熱容器を減圧スチームで加熱する装置であって、
前記減圧弁がその二次側の減圧程度により作動する逆負
荷をかけられた弁を有しており、前記スチームトラップ
がその一次側と二次側に絶えず連通ずるバイパスを備え
ていて、前記間接加熱容器へ常時安定した減圧スチーム
を供給するようにして成る減圧スチーム加熱装置。1 A pressure reducing valve and a steam trap are connected via an indirect heating container, and the steam supplied to the primary side of the pressure reducing valve is guided by a pressure reducing pump connected to the secondary side of the steam trap, thereby reducing the pressure of the pressure reducing valve. forming a desired reduced pressure system between the secondary side and the indirect heating vessel and the steam trap;
A device for heating an indirect heating container with reduced pressure steam,
The pressure reducing valve has an oppositely loaded valve activated by the degree of pressure reduction on its downstream side, and the steam trap has a bypass in constant communication with its primary and secondary sides, and A reduced pressure steam heating device that constantly supplies stable reduced pressure steam to a heating container.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17162383A JPS6064108A (en) | 1983-09-16 | 1983-09-16 | Decompression steam heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17162383A JPS6064108A (en) | 1983-09-16 | 1983-09-16 | Decompression steam heater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6064108A true JPS6064108A (en) | 1985-04-12 |
| JPH0465285B2 JPH0465285B2 (en) | 1992-10-19 |
Family
ID=15926605
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17162383A Granted JPS6064108A (en) | 1983-09-16 | 1983-09-16 | Decompression steam heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6064108A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS646603A (en) * | 1987-03-30 | 1989-01-11 | Tlv Co Ltd | Vacuum steam generator |
| FR2654817A1 (en) * | 1989-11-14 | 1991-05-24 | Tlv Co Ltd | THERMAL TREATMENT DEVICE, PARTICULARLY FOR THE CHEMICAL AND FOOD INDUSTRIES. |
| US5096538A (en) * | 1989-01-20 | 1992-03-17 | Fuji Photo Film Co., Ltd. | Vacuum drying method |
| JP2001324092A (en) * | 2000-05-15 | 2001-11-22 | Tlv Co Ltd | Condensate discharge device |
| GB2468562A (en) * | 2009-03-12 | 2010-09-15 | Lg Hausys Ltd | Decoration sheet having integrated printed and embossed patterns. |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4816660U (en) * | 1971-03-17 | 1973-02-24 | ||
| JPS4949232A (en) * | 1972-09-14 | 1974-05-13 | ||
| JPS5454330A (en) * | 1977-10-11 | 1979-04-28 | Tokico Ltd | Pilot valve |
| JPS575717U (en) * | 1980-06-10 | 1982-01-12 |
-
1983
- 1983-09-16 JP JP17162383A patent/JPS6064108A/en active Granted
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4816660U (en) * | 1971-03-17 | 1973-02-24 | ||
| JPS4949232A (en) * | 1972-09-14 | 1974-05-13 | ||
| JPS5454330A (en) * | 1977-10-11 | 1979-04-28 | Tokico Ltd | Pilot valve |
| JPS575717U (en) * | 1980-06-10 | 1982-01-12 |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS646603A (en) * | 1987-03-30 | 1989-01-11 | Tlv Co Ltd | Vacuum steam generator |
| US5096538A (en) * | 1989-01-20 | 1992-03-17 | Fuji Photo Film Co., Ltd. | Vacuum drying method |
| FR2654817A1 (en) * | 1989-11-14 | 1991-05-24 | Tlv Co Ltd | THERMAL TREATMENT DEVICE, PARTICULARLY FOR THE CHEMICAL AND FOOD INDUSTRIES. |
| NL8902936A (en) * | 1989-11-14 | 1991-06-17 | Tlv Co Ltd | THERMAL TREATMENT DEVICE. |
| JP2001324092A (en) * | 2000-05-15 | 2001-11-22 | Tlv Co Ltd | Condensate discharge device |
| GB2468562A (en) * | 2009-03-12 | 2010-09-15 | Lg Hausys Ltd | Decoration sheet having integrated printed and embossed patterns. |
| GB2468562B (en) * | 2009-03-12 | 2013-05-29 | Lg Hausys Ltd | Decoration sheet having integrated printed pattern and embossed pattern and manufacturing method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0465285B2 (en) | 1992-10-19 |
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