JPS6333413B2 - - Google Patents
Info
- Publication number
- JPS6333413B2 JPS6333413B2 JP1147581A JP1147581A JPS6333413B2 JP S6333413 B2 JPS6333413 B2 JP S6333413B2 JP 1147581 A JP1147581 A JP 1147581A JP 1147581 A JP1147581 A JP 1147581A JP S6333413 B2 JPS6333413 B2 JP S6333413B2
- Authority
- JP
- Japan
- Prior art keywords
- autoclave
- steam
- autoclaves
- cooled
- heated
- 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
Links
- 239000002699 waste material Substances 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000011381 foam concrete Substances 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000004567 concrete Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000011449 brick Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B40/00—Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
- C04B40/02—Selection of the hardening environment
- C04B40/024—Steam hardening, e.g. in an autoclave
-
- 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
- B01J3/04—Pressure vessels, e.g. autoclaves
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
Description
【発明の詳細な説明】
本発明は、被冷却オートクレーブからの廃汽を
被加熱オートクレーブへと移し、次に生蒸気を高
圧下被加熱オートクレーブに供給する特に泡コン
クリート硬化用の複数個のオートクレーブを運転
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a plurality of autoclaves, particularly for curing foam concrete, in which waste steam from a cooled autoclave is transferred to a heated autoclave, and then live steam is fed under high pressure to the heated autoclave. Regarding how to drive.
泡コンクリートを製造する場合硬化は複数個の
並列配置したオートクレーブ内で行われる。しか
しそのさい加熱と冷却は、すべてのオートクレー
ブで同時には行われず、ボイラー装置から長時間
にわたつて均一に同量の蒸気が取り出しうるよう
ずらされている。そのさい、普通、一方のオート
クレーブの廃汽は冷却時同時に他方のオートクレ
ーブを排気加熱するのに利用される(ラインスド
ルフ著『軽コンクリート』第2巻『多孔コンクリ
ート』、141、142頁、フアウ・エー・ベー・フエ
アラーク・フユア・バウヴエーゼン、ベルリン、
1963年刊参照)。しかし被冷却オートクレーブか
らの廃汽は両オートクレーブ内で同じ圧力が支配
するまでの間だけ被加熱オートクレーブに移しう
る。公知の方法では次に被加熱オートクレーブに
生蒸気が供給され、被冷却オートクレーブの残留
廃汽は、1部は給水を温めるためボイラー室へと
排出され、1部は大気中に放出される。したがつ
て廃汽エネルギーはそのごく僅かが利用されるに
すぎない。 When producing foam concrete, curing takes place in several autoclaves arranged in parallel. However, heating and cooling are not carried out simultaneously in all autoclaves, but are staggered so that the same amount of steam can be withdrawn uniformly from the boiler unit over a long period of time. In this case, the waste steam from one autoclave is usually used to exhaust heat the other autoclave at the same time as it cools down (Reinsdorf, Light Concrete, Vol. 2, Porous Concrete, pp. 141, 142, Fau. A.B. Verlag Fuur Bauwesen, Berlin;
(see 1963 publication). However, the waste steam from the cooled autoclave can only be transferred to the heated autoclave until the same pressure prevails in both autoclaves. In the known method, live steam is then supplied to the heated autoclave, and the residual waste steam of the cooled autoclave is partly discharged into the boiler room for heating the feed water and partly discharged into the atmosphere. Therefore, only a small amount of waste steam energy is utilized.
そこで本発明の課題は、被冷却オートクレーブ
の廃汽を簡単な手段でうまく利用する特に冒頭述
べた種類の泡コンクリート硬化用の複数個のオー
トクレーブを運転する方法を提供することであ
る。 SUMMARY OF THE INVENTION It is therefore an object of the present invention to provide a method for operating a plurality of autoclaves for curing foam concrete, in particular of the type mentioned at the outset, which makes good use of the waste steam of the cooled autoclaves in a simple manner.
この課題は本発明により、生蒸気を噴射蒸気と
して蒸気エゼクタ内を通し、該エゼクタの吸込側
を少なくとも加熱周期の1部の被冷却オートクレ
ーブと結合することによつて達成される。 This object is achieved according to the invention by passing the live steam as injection steam through a steam ejector, the suction side of which is connected to the cooled autoclave for at least part of the heating cycle.
本発明方法では生蒸気は、被冷却オートクレー
ブからの付加的廃汽を吸込んで被加熱オートクレ
ーブ内に送るのに利用される。生蒸気はいずれに
せよ被加熱オートクレーブに導入されねばならず
また蒸気エゼクタは比較的簡単に製造できる器械
であるから、両オートクレーブでの均圧後被冷却
オートクレーブ内になお残存する廃汽の大部分は
被加熱オートクレーブ内でひき続いて利用しう
る。これによつてエネルギー利用が改善される。 In the process of the invention, live steam is utilized to draw in additional waste steam from the cooled autoclave and pass it into the heated autoclave. Since the live steam must in any case be introduced into the heated autoclave and the steam ejector is a relatively simple device to manufacture, most of the waste steam still remaining in the cooled autoclave after pressure equalization in both autoclaves. can be used continuously in a heated autoclave. This improves energy utilization.
本方法は好ましくは次のように実施される。す
なわち、両オートクレーブ内で圧力が均衡するま
で蒸気を被冷却オートクレーブから被加熱オート
クレーブへと直接管を介して移し、その後はじめ
て被冷却オートクレーブを蒸気エゼクタの吸込側
と結合する。この方法は、複数個のオートクレー
ブにおいて別のオートクレーブの廃汽を供給する
蒸気エゼクタが使用でき、他のオートクレーブか
らの廃汽も直接管を介し被加熱オートクレーブ内
に流れ込むという利点を有している。 The method is preferably carried out as follows. This means that the steam is transferred directly from the cooled autoclave to the heated autoclave via a pipe until the pressures are balanced in both autoclaves, and only then is the cooled autoclave connected to the suction side of the steam ejector. This method has the advantage that in several autoclaves steam ejectors can be used which supply the waste steam of other autoclaves, and the waste steam from the other autoclaves also flows directly into the autoclave to be heated.
本発明方法を以下図示のフローシートに基づき
詳しく説明する。 The method of the present invention will be explained in detail below based on the illustrated flow sheet.
本図面には簡略化のため複数個のオートクレー
ブのうちただ2つがあらわしてある。この2つの
オートクレーブに関する以下の説明は同じ管路系
に接続されているその他のオートクレーブにもそ
のままあてはまる。オートクレーブ1はあふれ管
3を介しオートクレーブ2と結合されている。各
オートクレーブ1,2のためあふれ管内に弁4,
5が設けてある。更に、各オートクレーブ1,2
に付置された弁7,8によつて遮断しうる送り管
6が各オートクレーブ1,2に通じている。図示
省略した蒸気ボイラーから通じた生蒸気管9は弁
10を間挿して蒸気エゼクタ11に接続し、該エ
ゼクタの出口は送り管6と結合している。更に、
あふれ管3は結合管12を介し別の弁13を間挿
して蒸気エゼクタ11の吸込側と結合している。
更に、弁14によつて遮断可能な残留蒸気管15
が結合管12に設けてある。 For the sake of simplicity, only two of the autoclaves are shown in this drawing. The following description regarding these two autoclaves also applies exactly to the other autoclaves connected to the same line system. The autoclave 1 is connected to an autoclave 2 via an overflow pipe 3. Valve 4 in the overflow pipe for each autoclave 1, 2,
5 is provided. Furthermore, each autoclave 1, 2
A feed line 6 leads to each autoclave 1, 2, which can be shut off by a valve 7, 8 located therein. A live steam pipe 9 leading from a steam boiler (not shown) is connected to a steam ejector 11 through a valve 10, and the outlet of the ejector is connected to the feed pipe 6. Furthermore,
The overflow pipe 3 is connected to the suction side of the steam ejector 11 via a connecting pipe 12 with a further valve 13 interposed therebetween.
Furthermore, a residual steam line 15 which can be shut off by means of a valve 14
is provided in the coupling tube 12.
圧力をうけている左側のオートクレーブ1を冷
却し、右側の無圧のオートクレーブ2を加熱する
ものと仮定する。まずすべての弁は閉じており、
次に弁4が開かれ、弁5がゆつくり開かれる。長
い時間の間にオートクレーブ1からの廃汽はほぼ
均圧が成立するまでいまや結合管3を介しオート
クレーブ2に直接流れ込む。均圧が成立するや弁
5が閉じられ、弁8が開かれる。弁10がゆつく
り開くと生蒸気は噴射蒸気となつて蒸気エゼクタ
11内に流れうる。弁13が開かれるや、生蒸気
は蒸気エゼクタ11によつてオートクレーブから
のその他の廃汽を吸込み、該廃汽は生蒸気と一緒
にオートクレーブ2に達する。こうして、オート
クレーブ1に残存する廃汽の約20%が被加熱オー
トクレーブ2にポンピングされうる。 It is assumed that the pressurized left autoclave 1 is to be cooled, and the right autoclave 2, which is unpressurized, is to be heated. First, all valves are closed,
Valve 4 is then opened and valve 5 is slowly opened. Over a long period of time, the waste steam from the autoclave 1 now flows directly into the autoclave 2 via the connecting pipe 3 until an approximately equal pressure is established. Once the pressure is equalized, valve 5 is closed and valve 8 is opened. When the valve 10 is slowly opened, the live steam can flow into the steam ejector 11 as jet steam. Once the valve 13 is opened, the live steam sucks in other waste steam from the autoclave by the steam ejector 11, which reaches the autoclave 2 together with the live steam. Approximately 20% of the waste steam remaining in the autoclave 1 can thus be pumped into the heated autoclave 2.
オートクレーブ2内の背圧が高まることによつ
て蒸気エゼクタ11はその働きが次第に弱まり、
被冷却オートクレーブ1からの廃汽はもはやポン
ピングしえなくなる。いまや弁13が閉じられ、
弁14が開かれる。オートクレーブ1に残存する
残留蒸気は公知の方法でボイラー室内の給水を温
めるため残留蒸気管15を通して熱交換器へと供
給されうる、または排気函を介して大気中に放出
されうる。オートクレーブ2の加熱はいまや生蒸
気によつてのみ行われる。 As the back pressure inside the autoclave 2 increases, the steam ejector 11 gradually weakens.
The waste steam from the cooled autoclave 1 can no longer be pumped. Valve 13 is now closed,
Valve 14 is opened. The residual steam remaining in the autoclave 1 can be fed in a known manner to a heat exchanger through a residual steam line 15 for warming the feed water in the boiler room, or can be discharged into the atmosphere via an exhaust box. The autoclave 2 is now heated only by live steam.
オートクレーブ2を冷却し、オートクレーブ1
を加熱する場合同じ導管によつて本装置が逆の系
列においても運転しうることをあらわしたのが第
2図である。これは逆向きの矢印で示唆してあ
る。上述の順序に従つて各種の弁が開かれるが、
この順序は第2図にあらわした逆運転にも同様に
適用できる。 Cool autoclave 2, then autoclave 1.
FIG. 2 shows that the device can also be operated in the reverse series using the same conduit for heating. This is indicated by an arrow pointing in the opposite direction. The various valves are opened according to the above-mentioned order,
This sequence is equally applicable to the reverse operation shown in FIG.
本発明方法はもちろん泡コンクリート製造用オ
ートクレーブの運転だけでなく、製品を蒸気で処
理するところではどこでも適用でき、例えば珪灰
れんが用オートクレーブの運転にも適用できる。 The method of the invention can of course be applied not only to the operation of autoclaves for the production of foam concrete, but also wherever products are treated with steam, for example to the operation of autoclaves for silica bricks.
第1図は右側オートクレーブ2の加熱を示し、
第2図は左側オートクレーブ1の加熱をあらわす
フローシートである。
1,2……オートクレーブ、11……蒸気エゼ
クタ。
Figure 1 shows the heating of the right autoclave 2,
FIG. 2 is a flow sheet showing the heating of the left autoclave 1. 1, 2...autoclave, 11...steam ejector.
Claims (1)
ートクレーブへと移し、次に生蒸気を高圧下被加
熱オートクレーブに供給する特に泡コンクリート
硬化用の複数個のオートクレーブを運転する方法
において、生蒸気を噴射蒸気として蒸気エゼクタ
内を通し、該エゼクタの吸込側を少なくとも加熱
周期の1部の被冷却オートクレーブと結合するこ
とを特徴とする方法。 2 両オートクレーブ内で圧力が均衡するまで蒸
気を被冷却オートクレーブから被加熱オートクレ
ーブへと直接管を介して移し、その後はじめて被
冷却オートクレーブを蒸気エゼクタの吸込側と結
合することを特徴とする特許請求の範囲第1項記
載の方法。[Claims] 1. In a method for operating a plurality of autoclaves, especially for curing foam concrete, in which waste steam from a cooled autoclave is transferred to a heated autoclave, and then live steam is supplied to the heated autoclave under high pressure. , passing the live steam as injection steam through a steam ejector, the suction side of which is coupled to the cooled autoclave for at least part of the heating cycle. 2. A patent claim characterized in that the steam is transferred directly from the cooled autoclave to the heated autoclave via a pipe until the pressures are balanced in both autoclaves, and only then the cooled autoclave is connected to the suction side of the steam ejector. The method described in Scope 1.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19803010337 DE3010337C2 (en) | 1980-03-18 | 1980-03-18 | Process for the operation of several autoclaves, especially for the hardening of aerated concrete |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56130216A JPS56130216A (en) | 1981-10-13 |
JPS6333413B2 true JPS6333413B2 (en) | 1988-07-05 |
Family
ID=6097539
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1147581A Granted JPS56130216A (en) | 1980-03-18 | 1981-01-28 | Method of operating plurality of autoclave particularly for hardening bubble concrete |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS56130216A (en) |
DE (1) | DE3010337C2 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3210695C2 (en) * | 1982-03-24 | 1985-06-05 | Fels-Werke Peine-Salzgitter Gmbh, 3380 Goslar | Process for operating several autoclaves, especially for hardening aerated concrete |
DE3227097A1 (en) * | 1982-07-20 | 1984-01-26 | Ytong AG, 8000 München | METHOD FOR STEAM TREATMENT OF SEVERAL AUTOCLAVES AND DEVICE FOR IMPLEMENTING THE METHOD |
JP2888709B2 (en) * | 1992-10-29 | 1999-05-10 | 株式会社日立製作所 | How to replace a chemical reaction vessel in a chemical plant |
DE19541866C2 (en) * | 1995-11-09 | 2001-02-22 | Ytong Ag | Process for the hydrothermal hardening and drying of CSH-bound moldings and device for carrying out the process |
DE19608974C1 (en) * | 1996-03-08 | 1997-03-06 | Sicowa Verfahrenstech | Drying charge in high pressure steam autoclave |
DE69943147D1 (en) * | 1998-06-04 | 2011-03-03 | Denki Kagaku Kogyo Kk | HIGH-TEMPERATURE HIGH-PRESSURE UNDERWATER BEETON CURING DEVICE AND CURING PROCESS USING THE HARDENING DEVICE |
DE19932403B4 (en) * | 1999-07-14 | 2008-09-18 | Arnold Boroske | Method for autoclave evacuation for autogenous porous body or sand-lime brick production, autoclave system and use of an injector jet pump |
CA2541035A1 (en) * | 2006-03-27 | 2007-09-27 | Brian H. Harrison | Reactor for rubber reduction |
EP2165754A1 (en) * | 2008-05-13 | 2010-03-24 | Neuweiler AG | Autoclaves for the production of solar glasses and assembly with such autoclaves |
DE102010004747C5 (en) * | 2010-01-14 | 2014-11-13 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Process and plant for the hydrothermal hardening of moldings |
-
1980
- 1980-03-18 DE DE19803010337 patent/DE3010337C2/en not_active Expired
-
1981
- 1981-01-28 JP JP1147581A patent/JPS56130216A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
DE3010337B1 (en) | 1981-08-06 |
DE3010337C2 (en) | 1982-05-19 |
JPS56130216A (en) | 1981-10-13 |
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