JP3329683B2 - Recycling system for molding sand - Google Patents

Recycling system for molding sand

Info

Publication number
JP3329683B2
JP3329683B2 JP05410397A JP5410397A JP3329683B2 JP 3329683 B2 JP3329683 B2 JP 3329683B2 JP 05410397 A JP05410397 A JP 05410397A JP 5410397 A JP5410397 A JP 5410397A JP 3329683 B2 JP3329683 B2 JP 3329683B2
Authority
JP
Japan
Prior art keywords
sand
collected
cooling
mold
dust collector
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 - Lifetime
Application number
JP05410397A
Other languages
Japanese (ja)
Other versions
JPH10230342A (en
Inventor
邦保 森
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.)
Sintokogio Ltd
Original Assignee
Sintokogio Ltd
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 Sintokogio Ltd filed Critical Sintokogio Ltd
Priority to JP05410397A priority Critical patent/JP3329683B2/en
Publication of JPH10230342A publication Critical patent/JPH10230342A/en
Application granted granted Critical
Publication of JP3329683B2 publication Critical patent/JP3329683B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
  • Molds, Cores, And Manufacturing Methods Thereof (AREA)
  • Casting Devices For Molds (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、鋳型造型工程、注
湯工程、冷却工程、鋳型砂と素材の分離バラシ工程によ
る素材の取り出し及び鋳型砂の回収、回収鋳型砂の前処
理工程、回収砂の冷却工程、冷却回収砂の貯蔵混練処理
工程、混練砂の鋳型造型工程への供給を順次成す鋳型造
型砂の循環回収システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing a material and recovering a molding sand by a molding process, a pouring process, a cooling process, a separating process for separating the molding sand from the material, a pretreatment process for the recovered molding sand, and a recovered sand. The present invention relates to a circulating and collecting system for mold molding sand, which sequentially performs a cooling process, a storage and kneading process of cooling and collecting sand, and a supply of the kneaded sand to the mold making process.

【0002】[0002]

【従来の技術】従来上記のような鋳型造型砂の循環回収
システムにおいては、鋳型砂と素材の分離バラシ工程か
ら冷却回収砂の混練工程の間においてそれぞれ発生する
微粉を大型集塵機と多くの吸引ダクトを介して集塵する
と共に集塵された微粉を混練処理工程へ直接戻し入れる
ようにしている。
2. Description of the Related Art Conventionally, in a circulation system for collecting molding sand as described above, fine powder generated during a process of separating the molding sand from the material and a process of kneading the cooling and collecting sand is separated into a large dust collector and many suction ducts. And the collected fine powder is directly returned to the kneading process.

【0003】[0003]

【発明が解決しようとする課題】上記のように鋳型造型
砂の循環回収システムにおいて各所で発生する微粉を集
塵して混練工程へ戻し入れる場合、常に同じ鋳型が流れ
ていれば問題ないが、サンド/メタル比が異なる鋳型が
順次流れるものにおいては、各所で発生し集塵される微
粉の量、微粉の粒度分布、あるいは混練前の貯蔵された
回収砂の微粉含有量等がそれぞれ異なるようになり、混
練工程に対して集塵した微粉を定量供給しても混練され
た砂の微粉の含有量が異なることになり、これに伴って
混練砂の水分値、コンパクタビリティー値、通気度等の
砂特性が変わってしまい均一な品質の混練砂を得ること
ができないという問題があつた。また微粉の発生する場
所により大気温度及び湿度が大きく異なることから温度
及び湿度差がある空気が多くのダクトにより吸引されて
合流されるとその合流点において結露を起してダクトを
閉塞させてしまう問題があった。本発明は上記の問題に
鑑みて成されたもので、回収されて冷却、混練される鋳
型造型砂の微粉含有量を所定値に維持できると共に集塵
機の結露によるダクト閉塞をなくすことができる鋳型造
型砂の循環回収システムを提供することを目的とする。
As described above, when collecting and returning the fine powder generated in various places in the circulation system for mold molding sand to the kneading process as described above, there is no problem if the same mold always flows. In the case where molds with different sand / metal ratios flow sequentially, the amount of fine powder generated and collected in various places, the particle size distribution of fine powder, or the fine powder content of collected sand stored before kneading should be different. Therefore, even if the fine powder collected in the kneading process is supplied in a fixed amount, the content of the fine powder in the kneaded sand will be different, and accordingly, the moisture value of the kneaded sand, the compactability value, the air permeability, etc. There is a problem that the sand characteristics of the varnish vary and it is not possible to obtain kneaded sand of uniform quality. In addition, since the atmospheric temperature and humidity greatly differ depending on the place where the fine powder is generated, if air having a temperature and humidity difference is sucked and joined by many ducts, dew condensation occurs at the joining point and the duct is closed. There was a problem. The present invention has been made in view of the above-mentioned problems, and it is possible to maintain a fine powder content of a collected and cooled and kneaded mold molding sand at a predetermined value and to eliminate a duct blockage due to dew condensation of a dust collector. It is intended to provide a sand circulation recovery system.

【0004】[0004]

【課題を解決するための手段】上記の目的を達成するた
めに本発明における鋳型造型砂の循環回収システムは、
鋳型造型工程、注湯工程、冷却工程、鋳型砂と素材の分
離バラシ工程による素材の取り出し及び鋳型砂の回収、
回収鋳型砂の前処理工程、前処理済回収砂の冷却工程、
冷却砂の貯蔵混練処理工程、混練砂の鋳型造型工程への
砂供給を順次成す鋳型造型砂の循環回収システムにおい
て、前記鋳型砂と素材の分離バラシ工程及び回収砂の前
処理工程の各所において発生する微粉を第1集塵機によ
り集塵すると共に集塵された微粉を定量切り出しにより
前記回収砂の冷却工程の直前位置において元砂である回
収砂中に戻し入れ、前記回収砂の冷却工程を水の添加と
第2集塵機による吸引通風により成さしめもって該第2
集塵機による吸引微粉の全量を冷却済の元砂である回収
砂中に戻し入れ、かつ前記冷却回収砂の貯蔵混練処理工
程の各所で発生する微粉を第3集塵機により集塵して廃
砂にすることを特徴とするものである。
Means for Solving the Problems In order to achieve the above-mentioned object, a circulation and recovery system for molding sand in the present invention is provided.
Material removal and mold sand recovery by mold making process, pouring process, cooling process, mold sand and material separation process,
Pretreatment process of recovered mold sand, cooling process of pretreated recovered sand,
In the circulation and recovery system of the molding sand, which successively supplies the sand to the storage and kneading treatment process of the cooling sand and the kneading sand to the molding process of the molding sand, the sand is generated at various places in the separation and separation process of the molding sand and the material and the pretreatment process of the recovered sand. The collected fine powder is collected by the first dust collector, and the collected fine powder is returned to the original sand at a position immediately before the cooling step of the collected sand by quantitative cutout, and the cooling step of the collected sand is performed by the water collecting step. Addition and suction by a second dust collector to form the second dust collector.
The whole amount of fine powder sucked by the dust collector is returned to the recovered sand as cooled original sand, and the fine powder generated in various places in the storage and kneading process of the cooled recovered sand is collected by a third dust collector to be waste sand. It is characterized by the following.

【0005】[0005]

【発明の実施の形態】以下本発明の実施の形態を図面に
基づいて詳しく説明する。図1において鋳型造型砂の循
環回収は、鋳型造型工程1、注湯工程2、冷却工程3、
冷却鋳型の鋳型砂と素材(鋳造品)の分離バラシ工程
4、回収鋳型砂の鉄片分離マグネットセパレータ5A、
第1鋳型砂搬送コンベヤ5B、荒ふるい5Cより成る回
収鋳型砂の前処理工程5、前処理済回収砂の冷却工程
6、冷却砂の第2砂搬送コンベヤ7A、サンドストレー
ジ7B、第3砂搬送コンベヤ7C、冷却砂の混練機7
D、より成る冷却砂の貯蔵混練処理工程7、混練砂の鋳
型造型工程1への砂供給を順次成す基本ラインが構成さ
れている。
Embodiments of the present invention will be described below in detail with reference to the drawings. In FIG. 1, the circulation and recovery of the molding sand are performed in a molding process 1, a pouring process 2, a cooling process 3,
Separation process 4 of the mold sand of the cooling mold and the material (casting product), a magnet separator 5A for separating iron pieces of the recovered mold sand,
Pre-processing step 5 of recovered mold sand composed of a first mold sand transport conveyor 5B and a coarse sieve 5C, cooling step 6 of pre-processed recovered sand, second sand transport conveyor 7A for cooling sand, sand storage 7B, third sand transport Conveyor 7C, Cooling sand kneader 7
D, a basic line for sequentially supplying the sand to the cooling sand storage / kneading step 7 and the kneading sand to the mold forming step 1.

【0006】この基本ラインにおいて鋳型砂と素材の分
離バラシ工程4とこれに続く鉄片分離マグネットセパレ
ータ5A、第1砂搬送コンベヤ5B、荒ふるい5Cより
成る回収鋳型砂の前処理工程5の各所はそれぞれ第1集
塵機11にダクト12を介して連通されて微粉の集塵が
なされるようにされている。該第1集塵機11で集塵さ
れた微粉はクッションホッパ13に溜められ定量微粉切
り出機14により切り出されて前記回収砂冷却工程6の
直前位置において回収砂にもどされるようにされてい
る。なおクッションホッパ13からオーバフローした微
粉は廃砂されるようになっている。すなわち鋳型砂が高
温状態にある分離バラシ工程4及び回収砂前処理工程5
の各所で発生する乾燥した微粉は第1集塵機11により
集塵回収されて冷却前の元砂である回収砂に定量供給に
よりもどされる。
In this basic line, each part of a separation step 4 for separating mold sand and material, followed by a pretreatment step 5 for recovered mold sand comprising a magnet separator 5A, a first sand conveyor 5B, and a rough sieve 5C, which follows. The first dust collector 11 is communicated via a duct 12 to collect fine dust. The fine powder collected by the first dust collector 11 is stored in a cushion hopper 13, cut out by a fixed-quantity fine-powder cutting machine 14, and returned to the collected sand at a position immediately before the collected sand cooling step 6. The fine powder overflowing from the cushion hopper 13 is to be wasted. That is, the separation and dispersion step 4 and the recovered sand pretreatment step 5 in which the mold sand is in a high temperature state.
The dried fine powder generated in each place is collected and collected by the first dust collector 11 and is returned to the collected sand, which is the original sand before cooling, by a quantitative supply.

【0007】次に、前処理工程5を済ませると共に乾燥
した微粉を戻された回収砂は水の添加をうけながら第2
集塵機15による吸引通風により冷却される一方第2集
塵機15により吸引された正常砂粒を含む微粉は戻しコ
ンベヤ16を介して冷却後の元砂である回収砂へ戻され
る。回収砂に水を添加して効果的に冷却するためには第
2集塵機15の吸引風量を高くして高速で空気を回収砂
に通過接触させる必要があり、このことから正常な砂粒
の砂をも一部吸引されるようになり、この正常の砂粒を
含む吸引微粉は全て冷却後の元砂である回収砂に直ちに
もどされる。さらに冷却後の回収砂は第2砂搬送コンベ
ヤ7A、サンドストレージ7B、第3砂搬送コンベヤ7
C、混練機7Dより成る冷却砂の貯蔵混練処理工程7の
各所がそれぞれ第3集塵機17にダクト18を介して連
通されて、発生する低温多湿の微粉及び空気が集塵され
るようになっており、第3集塵機17で集塵された微粉
はその回収量が少ない(湿態のため発塵しにくい)と共
に結露による障害をなくすために他の機器を通過させず
に廃棄するようにしている。
[0007] Next, after the pretreatment step 5, the recovered sand from which the dried fine powder has been returned is subjected to a second addition while receiving water.
The fine powder containing the normal sand particles sucked by the second dust collector 15 while being cooled by the suction ventilation by the dust collector 15 is returned to the recovered sand which is the original sand after cooling via the return conveyor 16. In order to add water to the collected sand and cool it effectively, it is necessary to increase the suction air volume of the second dust collector 15 and allow the air to pass through and contact the collected sand at a high speed. Some of the fine suction powder containing normal sand grains is immediately returned to the recovered sand which is the original sand after cooling. Further, the collected sand after cooling is supplied to the second sand conveyor 7A, the sand storage 7B, the third sand conveyor 7
C, each part of the cooling sand storage and kneading treatment step 7 comprising the kneading machine 7D is connected to the third dust collector 17 via the duct 18 so that the generated low-temperature and high-humidity fine powder and air are collected. The fine dust collected by the third dust collector 17 has a small recovery amount (it is difficult to generate dust due to the wet state) and is disposed of without passing through other devices in order to eliminate an obstacle due to dew condensation. .

【0008】[0008]

【発明の効果】本発明は上記の説明から明らかなよう
に、微粉の発生する全ての場所で集塵が成され、高温乾
燥状態の微粉は元砂である冷却前の回収砂中に戻され、
水の添加と集塵機の吸引によって冷却される回収砂の正
常砂粒を一部含む微粉は直ちに元砂である冷却後の回収
砂中に全量が戻され、さらに低温多湿で集塵されて結露
の恐れがある少量の微粉は他の機器を通過させずに廃棄
されるため、発生した微粉は全て元砂に戻されるように
なり、砂性状を変えることなく混練されて、その水分
値、コンパクタビリティー値等を大きく変えることなく
均一な品質の混練砂として鋳型造型工程へ送り出すこと
ができるとともに集塵機の結露がなくなる等優れた効果
がある。
As is clear from the above description, the present invention collects dust at all places where fine powder is generated, and returns fine powder in a high-temperature dry state to recovered sand before cooling, which is original sand. ,
The fine powder containing a part of the normal sand of the recovered sand cooled by the addition of water and the suction of the dust collector is immediately returned to the original sand, which is the recovered sand after cooling, and the entire amount is collected. Since a small amount of fine powder is discarded without passing through other equipment, all the generated fine powder is returned to the original sand, kneaded without changing the sand properties, and its moisture value, compactability It has excellent effects such as being able to be sent to the mold making process as a kneaded sand of uniform quality without greatly changing the value and the like, and having no dew condensation in the dust collector.

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

【図1】本発明の実施例を示すフローチャート図であ
る。
FIG. 1 is a flowchart illustrating an embodiment of the present invention.

【符号の説明】 4 鋳型砂と素材の分離バラシ工程 5 前処理工程 6 回収砂の冷却工程 7 貯蔵混練処理工程 11 第1集塵機 15 第2集塵機 17 第3集塵機[Description of Signs] 4 Separation process of mold sand and material 5 Pretreatment process 6 Cooling process of recovered sand 7 Storage and kneading process 11 First dust collector 15 Second dust collector 17 Third dust collector

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 鋳型造型工程1、注湯工程2、冷却工程
3、鋳型砂と素材の分離バラシ工程4による素材の取り
出し及び鋳型砂の回収、回収鋳型砂の前処理工程5、前
処理済回収砂の冷却工程6、冷却砂の貯蔵混練処理工程
7、混練砂の鋳型造型工程1への砂供給を順次成す鋳型
造型砂の循環回収システムにおいて、前記鋳型砂と素材
の分離バラシ工程4及び回収砂の前処理工程5の各所に
おいて発生する微粉を第1集塵機11により集塵すると
共に集塵された微粉を定量切り出しにより前記回収砂の
冷却工程6の直前位置において元砂である回収砂中に戻
し入れ、前記回収砂の冷却工程6を水の添加と第2集塵
機15による吸引通風により成さしめもって該第2集塵
機15による吸引微粉の全量を冷却済の元砂である回収
砂中に戻し入れ、かつ前記冷却回収砂の貯蔵混練処理工
程7の各所で発生する微粉を第3集塵機18により集塵
して廃砂にすることを特徴とする鋳型造型砂の循環回収
システム。
1. A mold forming process 1, a pouring process 2, a cooling process 3, a material removal and a mold sand recovery by a mold sand and material separation / balancing process 4, a pre-process 5 of a recovered mold sand, a pre-processed In the system for recovering and cooling the recovered sand, the step of storing and kneading the cooled sand, the step 7 of storing and kneading the sand, and the step of supplying the sand to the step of forming the kneaded sand 1 in the circulation and recovery system of the molding sand, The fine dust generated in each part of the pre-processing step 5 of the collected sand is collected by the first dust collector 11 and the collected fine powder is cut out by quantitative cut-out at a position immediately before the cooling step 6 of the collected sand. The cooling step 6 of the collected sand is performed by adding water and sucking and drafting by the second dust collector 15 so that the whole amount of the fine powder sucked by the second dust collector 15 is collected into the recovered sand which is cooled original sand. Put it back 3. A circulating and collecting system for mold molding sand, characterized in that fine powder generated in various places in the storage and kneading treatment step 7 of the cooling and collecting sand is collected by a third dust collector 18 into waste sand.
JP05410397A 1997-02-21 1997-02-21 Recycling system for molding sand Expired - Lifetime JP3329683B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05410397A JP3329683B2 (en) 1997-02-21 1997-02-21 Recycling system for molding sand

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05410397A JP3329683B2 (en) 1997-02-21 1997-02-21 Recycling system for molding sand

Publications (2)

Publication Number Publication Date
JPH10230342A JPH10230342A (en) 1998-09-02
JP3329683B2 true JP3329683B2 (en) 2002-09-30

Family

ID=12961288

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05410397A Expired - Lifetime JP3329683B2 (en) 1997-02-21 1997-02-21 Recycling system for molding sand

Country Status (1)

Country Link
JP (1) JP3329683B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5316888B2 (en) * 2009-12-11 2013-10-16 新東工業株式会社 Method and system for treating harmful substances in mold sand
WO2011077771A1 (en) * 2009-12-26 2011-06-30 新東工業株式会社 Semiautomatic vacuum molding process casting line
CN102133616B (en) * 2011-03-08 2012-08-15 华中科技大学 Reclaiming method of mixed waste sand for casting

Also Published As

Publication number Publication date
JPH10230342A (en) 1998-09-02

Similar Documents

Publication Publication Date Title
CA2209381C (en) Process and plant for processing mixed plastics
JP3329683B2 (en) Recycling system for molding sand
JP2003111556A (en) Screening machine for tea processing
GB2250220A (en) Reclamation of additives from used sand
CN106238332B (en) Wood shaving sorting device
US3593851A (en) Tobacco leaf classifier
CN107737787A (en) A kind of processing method of rice processing tail dirt
WO2001064371A1 (en) Collected sand processing method
JP2007175683A (en) Pneumatic classifier and mixed waste treatment apparatus
CN105919153B (en) A kind of redrying cabo sifting process
KR20220087500A (en) Particle Separation Device for Additive Manufacturing and Additive Manufacturing Apparatus
JPS628256B2 (en)
CN202278659U (en) Dry-mixed mortar equipment and drying system thereof
JP2004188695A (en) Method for recycling waste polyolefins and system therefor
JP2002520513A (en) Knit separation equipment
CN210009724U (en) Workshop intelligence dust device
TW202039103A (en) Method for processing electronic/electrical device component scraps
CN208679807U (en) A kind of winnowing machine
JP2006192486A (en) Adjusting method and facility for adjusting recovered sand
CN203556407U (en) Bean huller
CN206065328U (en) A kind of cast tube antiquated sand retracting device
JPS6334901Y2 (en)
US20210206099A1 (en) Build material recovery for a three-dimensional (3d) printer
CN212550499U (en) Powder grading and collecting device
CN216002633U (en) Convenient conveyor is used in production of silica gel drier

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080719

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090719

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090719

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100719

Year of fee payment: 8