JPS5832640B2 - Freeze-thaw sludge treatment equipment - Google Patents

Freeze-thaw sludge treatment equipment

Info

Publication number
JPS5832640B2
JPS5832640B2 JP11202277A JP11202277A JPS5832640B2 JP S5832640 B2 JPS5832640 B2 JP S5832640B2 JP 11202277 A JP11202277 A JP 11202277A JP 11202277 A JP11202277 A JP 11202277A JP S5832640 B2 JPS5832640 B2 JP S5832640B2
Authority
JP
Japan
Prior art keywords
sludge
chamber
frozen
melting
freeze
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
Application number
JP11202277A
Other languages
Japanese (ja)
Other versions
JPS5445959A (en
Inventor
健一郎 山西
哲雄 森口
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 Electric Corp
Original Assignee
Mitsubishi Electric 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 Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP11202277A priority Critical patent/JPS5832640B2/en
Publication of JPS5445959A publication Critical patent/JPS5445959A/en
Publication of JPS5832640B2 publication Critical patent/JPS5832640B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は、汚泥を凍結したのち融解することによって
脱水性を向上させるようにした凍結融解式汚泥処理装置
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a freeze-thaw type sludge treatment apparatus that improves dewatering performance by freezing and then thawing sludge.

従来のこの種の汚泥処理装置を第1図に示す。A conventional sludge treatment apparatus of this type is shown in FIG.

第1図において、1は管軸方向に一定の管路断面を有し
、収容される汚泥(図示せず)を凍結する部分と融解す
る部分とからなる管体、2は複数本の管体1を収容する
筐体、3aおよび3bは筐体2によって上記管体1の凍
結部、融解部の周囲に形成される第1および第2の器室
、4は各々の器室3a 、3bに流れる図示しない冷却
媒体、加熱媒体を均一に上記管体1の外周面に接触させ
るための仕切板である。
In Fig. 1, 1 is a pipe body that has a constant cross section in the pipe axis direction, and consists of a part that freezes and a part that thaws the sludge (not shown) contained therein, and 2, a plurality of pipe bodies. 1, 3a and 3b are first and second chambers formed by the casing 2 around the freezing and thawing sections of the pipe body 1, and 4 is a housing for each chamber 3a, 3b. This is a partition plate for uniformly bringing the flowing cooling medium and heating medium (not shown) into contact with the outer peripheral surface of the tube body 1.

また、5および6は上記管体1の両端を各々開口した給
泥室および排泥室、7および8はこれら両室5,6に通
ずる給泥管および排泥管、9は上記管体1の排泥室6側
聞ロ部に設りられ、凍結した汚泥の移動を阻止するスト
ッパ、10は原汚泥を装置内に供給するための汚泥圧入
ポンプである。
Reference numerals 5 and 6 refer to a mud supply chamber and a mud removal chamber which are open at both ends of the pipe body 1, 7 and 8 a mud supply pipe and a mud discharge pipe that communicate with both chambers 5 and 6, and 9 a mud supply pipe and a mud discharge pipe that are open at both ends of the pipe body 1. A stopper 10 is installed in the side wall of the sludge discharge chamber 6 to prevent movement of frozen sludge, and 10 is a sludge injection pump for supplying raw sludge into the apparatus.

さらに、11は蒸発器11a、凝縮器11b、圧縮器1
1cおよび膨張弁11dを有する冷凍装置、12は上記
第1の器室3aと蒸発器11aとを結ぶ管路、13は上
記第2の器室3bと凝縮器11bとを結ぶ管路、14は
冷凍装置11内の冷媒回路、15は凍結汚泥の表面層融
解に用いられる加熱媒体用管路、16は凝縮器3bと後
述熱交換器を結ぶ管路、17は第1の器室3a内の熱媒
体を抜き取る管路、18はエアー抜き管路、19a〜1
9jは、これらの各管路12.13.15〜18に設け
られた開閉バルブ、20.21は熱媒体貯留槽、22〜
24はポンプ、25はクーリングタワー、26は熱交換
器である。
Furthermore, 11 is an evaporator 11a, a condenser 11b, a compressor 1
1c and an expansion valve 11d; 12 is a pipe connecting the first chamber 3a and the evaporator 11a; 13 is a pipe connecting the second chamber 3b and the condenser 11b; 14 is a pipe connecting the second chamber 3b and the condenser 11b; A refrigerant circuit in the refrigeration device 11, 15 a heating medium pipe line used for melting the surface layer of frozen sludge, 16 a pipe line connecting the condenser 3b and a heat exchanger to be described later, and 17 a pipe line in the first chamber 3a. Pipe line for extracting heat medium, 18 is air release pipe line, 19a to 1
9j is an on-off valve provided in each of these pipelines 12, 13, 15-18, 20.21 is a heat medium storage tank, 22-
24 is a pump, 25 is a cooling tower, and 26 is a heat exchanger.

このような従来装置において、バルブ19a〜19jお
よびポンプ22.23を操作して熱媒体を系内に循環さ
せると、蒸発器11aによって冷却された熱媒体は第1
の器室3aに流れて管体1内の第1の器室3aで囲まれ
た部分の原汚泥を凍結すると共に、凝縮器11bによっ
て加熱された熱媒体は第2の器室3bに流れて管体1内
の第2の器室3bで囲まれた部分の凍結汚泥を融解する
In such a conventional device, when the heat medium is circulated within the system by operating the valves 19a to 19j and the pumps 22.23, the heat medium cooled by the evaporator 11a is
The heat medium flows into the second chamber 3a and freezes the raw sludge in the part surrounded by the first chamber 3a in the tube body 1, and the heat medium heated by the condenser 11b flows into the second chamber 3b. The frozen sludge in the area surrounded by the second chamber 3b in the tube body 1 is thawed.

このように凍結、融解が完了した後、上記各バルブ19
a〜19jを再び操作すると熱媒体貯留槽21内の加熱
媒体は第1の器室3aに流れることとなり、管体1内の
第1の器室3aに囲まれた部分の凍結汚泥の表面層を極
く薄く融解して移動可能な状態とする。
After freezing and thawing are completed in this way, each of the valves 19
When a to 19j are operated again, the heating medium in the heating medium storage tank 21 will flow to the first chamber 3a, and the surface layer of frozen sludge in the part surrounded by the first chamber 3a in the pipe body 1 will be Melt it into a very thin layer and make it movable.

この状態から汚泥圧入ポンプ10によって原汚泥が供給
圧入されると、この原汚泥により凍結汚泥は管体1内を
汚泥供給側より汚泥排出側へ向けてストッパ9で停止さ
れる位置まで押し上げられて原汚泥の充填が完了すると
共に、先に管体1内の第2の器室3bで囲まれた部分で
融解されている汚泥は上記凍結汚泥の移動に伴って外部
に排出されることとなる。
When raw sludge is supplied from this state by the sludge injection pump 10, the frozen sludge is pushed up inside the tube 1 from the sludge supply side to the sludge discharge side until it is stopped by the stopper 9. When the filling of the raw sludge is completed, the sludge that has been previously thawed in the area surrounded by the second chamber 3b in the pipe body 1 will be discharged to the outside as the frozen sludge moves. .

以後再び上記各バルブ19a〜19jを切換操作するこ
とによって上述動作が繰り返され、汚泥の凍結、融解処
理がなされるものである。
Thereafter, the above-mentioned operations are repeated by switching the respective valves 19a to 19j again, and the sludge is frozen and thawed.

しかしながらこのような従来装置では、上述したように
汚泥の凍結および融解後、凍結汚泥の表面層の一部融解
をする場合に、第1の器室3a内で加熱媒体を一定方向
にのみ流すように管路構成され、また制御するようにな
っているため管体1の軸方向の熱媒体温度あるいは熱伝
達係数の不同によって凍結汚泥の表面層の融解が管軸方
向にむらになるに至る。
However, in such a conventional device, when the surface layer of the frozen sludge is partially thawed after freezing and thawing the sludge as described above, the heating medium is made to flow only in a certain direction within the first chamber 3a. Since the pipes are configured and controlled, the melting of the surface layer of frozen sludge becomes uneven in the axial direction of the tube due to differences in the heat medium temperature or heat transfer coefficient in the axial direction of the tube body 1.

このためある部分では必要以上に融解が進んで管体1の
内面と凍結汚泥の外面との間隙が大きくなっていても、
他の部分では全く融解していないことすらあり、凍結汚
泥が管体1上部側に移動を始める前に、圧入される原汚
泥が上記間隙を通して融解汚泥中に混入し易く、また、
凍結汚泥が管体1上部に移動し、ストッパ9で停止した
後にも同様に原汚泥が融解汚泥中に混入する場合がある
等の欠点があった。
Therefore, even if melting progresses more than necessary in a certain part and the gap between the inner surface of the tube body 1 and the outer surface of the frozen sludge becomes large,
Other parts may not even be melted at all, and before the frozen sludge begins to move to the upper side of the pipe body 1, the raw sludge that is press-in is likely to mix into the molten sludge through the above-mentioned gap, and
There is a problem that even after the frozen sludge moves to the upper part of the pipe body 1 and stops at the stopper 9, the raw sludge may be mixed into the molten sludge.

この発明は、凍結汚泥表面層の融解むらを少なくして上
記欠点を除去した凍結融解式汚泥処理装置を提供するこ
とを目的とする。
An object of the present invention is to provide a freeze-thaw type sludge treatment apparatus that eliminates the above-mentioned drawbacks by reducing uneven melting of the frozen sludge surface layer.

以下第2図ないし第4図を参照してこの発明の詳細な説
明する。
The present invention will be described in detail below with reference to FIGS. 2 to 4.

第2図はこの発明による凍結融解式汚泥処理装置の一実
施例を示す概略構成図、第3図は同上装置の要部の一例
を上方より示す断面図で、これら両図において、3cy
3dは加熱媒体を流す器室である。
Fig. 2 is a schematic configuration diagram showing an embodiment of the freeze-thaw sludge treatment apparatus according to the present invention, and Fig. 3 is a cross-sectional view showing an example of the main parts of the same apparatus from above.
3d is a chamber through which the heating medium flows.

その他の部分は第1図の場合と同様であるので同一部分
に同一符号を付してその説明を省略するが、この発明装
置では、管体1は水平状態に設置されている。
Since the other parts are the same as those in FIG. 1, the same parts are given the same reference numerals and the explanation thereof will be omitted. In the apparatus of this invention, the tube body 1 is installed in a horizontal state.

すなわちこの発明は、管体1を水平に置き、凍結汚泥の
表面層融解に用いる加熱媒体を、第1の器室3a内に加
熱媒体液面高さを水平に保持しながら充填し、また第1
の器室3aの両端部に器室3c 、3dを設け、この器
室3c 、3d内には冷却媒体は流さず加熱媒体のみを
流すようにしたものである。
That is, in this invention, the pipe body 1 is placed horizontally, and the heating medium used for melting the surface layer of frozen sludge is filled into the first chamber 3a while maintaining the liquid level of the heating medium horizontally. 1
Chambers 3c and 3d are provided at both ends of the chamber 3a, and no cooling medium is allowed to flow into these chambers 3c and 3d, but only a heating medium is allowed to flow therein.

上述この発明装置において、第2図および第3図に示す
ように管体1を水平に置く、従って仕切板4も図示する
ように配置することにより、まず凍結が完了した時点で
第1の器室3a内より冷却媒体を抜き取り、次に熱媒体
貯留槽21内の加熱媒体が第1の器室3a内にその液面
高さを水平に保持しながら充填されるようになることか
ら、1本の管体1の軸方向に対する加熱媒体の温度およ
び熱伝達係数のむらが少なくなって凍結汚泥の表面層の
融解むらが少な、、くなる。
In the above-mentioned apparatus of the present invention, by placing the tube body 1 horizontally as shown in FIGS. 2 and 3, and by arranging the partition plate 4 as shown, first, when freezing is completed, the first vessel The cooling medium is extracted from the chamber 3a, and then the heating medium in the heat medium storage tank 21 is filled into the first chamber 3a while maintaining the liquid level horizontally. The unevenness of the temperature and heat transfer coefficient of the heating medium in the axial direction of the tube body 1 is reduced, and the unevenness of melting of the surface layer of frozen sludge is reduced.

さらに第1の器室3aの両端部に器室3c 、3dを設
け、この器室3c 、3d内は、第1の器室3a内に冷
却媒体を流している時は空のままとし、凍結汚泥の表面
層のみを融解する時には加熱媒体を流す。
Further, chambers 3c and 3d are provided at both ends of the first chamber 3a, and these chambers 3c and 3d remain empty when the cooling medium is flowing into the first chamber 3a, and are frozen. When melting only the surface layer of sludge, a heating medium is flowed.

このようにすれば、表面層融解時に端部の熱伝達の悪さ
により生じる表面層融解時間が長くかかるという不具合
を解消することができ、凍結汚泥の移動が円滑になる。
In this way, it is possible to solve the problem that it takes a long time to melt the surface layer due to poor heat transfer at the edges when the surface layer is melted, and the movement of the frozen sludge becomes smooth.

第4図はこの発明の他の実施例の要部を側方より示す断
面図で、凍結時の熱伝達係数を上げるために仕切板4の
配置をかえたものであるが、この場合にも表面層融解用
のヘッダ27を取りつけることにより仕切板4でいくつ
かに仕切られた各室間の液面を同一に保持するように表
面層融解用の加熱媒体を充填することができ、上述実施
例と同様に表面層の融解むらを少なくすることができる
FIG. 4 is a sectional view showing the main part of another embodiment of the present invention from the side, in which the arrangement of the partition plate 4 is changed in order to increase the heat transfer coefficient during freezing. By attaching the header 27 for melting the surface layer, it is possible to fill the heating medium for melting the surface layer so as to maintain the same liquid level in each chamber partitioned into several by the partition plate 4. As in the example, uneven melting of the surface layer can be reduced.

なお、第4図において第3図と同様の部分には同一符号
を付した。
In FIG. 4, the same parts as in FIG. 3 are given the same reference numerals.

以上述べたようにこの発明によれば、管体1を水平に置
き、凍結汚泥の表面層融解のための加熱媒体を、その液
面高さを水平に保持しながら充填するようにしたので、
凍結汚泥表面層の融解むらを少なくすることができ、融
解汚泥中への原汚泥の混入を防止することができる。
As described above, according to the present invention, the pipe body 1 is placed horizontally and the heating medium for melting the surface layer of frozen sludge is filled while maintaining the liquid level horizontally.
Uneven melting of the surface layer of frozen sludge can be reduced, and mixing of raw sludge into molten sludge can be prevented.

また、第1の器室3aの両端部に、冷却媒体は流さずに
加熱媒体のみを流すようにした器室3c 93dを設け
ることによって凍結汚泥の移動を円滑にすることができ
るという効果がある。
Further, by providing chambers 3c to 93d at both ends of the first chamber 3a, through which only a heating medium is allowed to flow without a cooling medium, there is an effect that the movement of frozen sludge can be made smoother. .

【図面の簡単な説明】 第1図は従来装置の概略構成図、第2図はこの発明によ
る凍結融解式汚泥処理装置の一実施例を示す概略構成図
、第3図は同上装置の要部の一例を上方より示す断面図
、第4図はこの発明の他の実施例の要部を側方より示す
断面図である。 1・・・管体、3a 、 3b・・・第1および第2の
器室、3 c p 3 d・・・器室、10・・・汚泥
圧入ポンプ、11・・・冷凍装置、12,13.15〜
18・・・管路、19a〜19j・・・開閉バルブ、な
お、図中同一符号は同一または相当部分を示す。
[BRIEF DESCRIPTION OF THE DRAWINGS] Fig. 1 is a schematic configuration diagram of a conventional device, Fig. 2 is a schematic configuration diagram showing an embodiment of the freeze-thaw sludge treatment device according to the present invention, and Fig. 3 is a main part of the same device. FIG. 4 is a cross-sectional view showing an example from above, and FIG. 4 is a cross-sectional view showing main parts of another embodiment of the invention from the side. DESCRIPTION OF SYMBOLS 1... Pipe body, 3a, 3b... 1st and 2nd chamber, 3 c p 3 d... Container chamber, 10... Sludge injection pump, 11... Freezing device, 12, 13.15~
18... Pipes, 19a-19j... Opening/closing valves. In addition, the same reference numerals in the drawings indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】 1 管軸方向に一定の管路断面を有する管体と、この管
体の周囲の入口側および出口側に夫々設けられた第1お
よび第2の器室と、第1の器室で囲まれた管体内に原汚
泥を圧入する手段と、第1の器室に該器室に囲まれた管
体内の原汚泥を凍結させる冷却媒体を供給するとともに
この凍結汚泥の表面層を融解する加熱媒体を供給しかつ
第2の器室に該器室に囲まれた管体内に原汚泥の圧入に
より移動した凍結汚泥を融解する加熱媒体を供給する媒
体供給機構を備えた凍結融解式汚泥処理装置において、
上記管体を水平状態に設置するとともに、上記媒体供給
機構は凍結汚泥の表面層融解に用いる加熱媒体をその液
面高さが水平となるように第1の器室内に供給するよう
にしたことを特徴とする凍結融解式汚泥処理装置。 2 第1の器室の両端部分に、汚泥凍結時には空のまま
とし凍結汚泥の表面層融解時に加熱媒体を流すようにし
た器室を設けたことを特徴とする特許請求の範囲第1項
記載の凍結融解式汚泥処理装置。
[Scope of Claims] 1. A tube body having a constant pipe cross section in the tube axis direction, first and second chambers provided around the tube body on the inlet side and the outlet side, respectively, and a first chamber. a means for pressurizing raw sludge into a tube surrounded by a first chamber; a means for supplying a cooling medium to a first chamber to freeze the raw sludge in the tube surrounded by the first chamber; Freezer equipped with a medium supply mechanism for supplying a heating medium for melting a layer and for supplying a heating medium for melting frozen sludge that has been moved into a second vessel chamber by pressurizing raw sludge into a tube surrounded by the vessel chamber. In melting sludge treatment equipment,
The pipe body is installed in a horizontal state, and the medium supply mechanism is configured to supply the heating medium used for melting the surface layer of frozen sludge into the first chamber so that the liquid level is horizontal. Freeze-thaw sludge treatment equipment featuring: 2. Claim 1, characterized in that chambers are provided at both ends of the first chamber, the chambers being left empty when the sludge is frozen, and allowing a heating medium to flow through when the surface layer of the frozen sludge is thawing. Freeze-thaw sludge treatment equipment.
JP11202277A 1977-09-16 1977-09-16 Freeze-thaw sludge treatment equipment Expired JPS5832640B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11202277A JPS5832640B2 (en) 1977-09-16 1977-09-16 Freeze-thaw sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11202277A JPS5832640B2 (en) 1977-09-16 1977-09-16 Freeze-thaw sludge treatment equipment

Publications (2)

Publication Number Publication Date
JPS5445959A JPS5445959A (en) 1979-04-11
JPS5832640B2 true JPS5832640B2 (en) 1983-07-14

Family

ID=14576018

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11202277A Expired JPS5832640B2 (en) 1977-09-16 1977-09-16 Freeze-thaw sludge treatment equipment

Country Status (1)

Country Link
JP (1) JPS5832640B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6347923A (en) * 1986-08-18 1988-02-29 Fujitsu Ltd Structure of heat treatment furnace

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110986481A (en) * 2019-12-20 2020-04-10 盐城威布三维科技有限公司 Cooling mechanism for 3D printer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6347923A (en) * 1986-08-18 1988-02-29 Fujitsu Ltd Structure of heat treatment furnace

Also Published As

Publication number Publication date
JPS5445959A (en) 1979-04-11

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