JPH05309726A - Fluid compression recycling apparatus - Google Patents

Fluid compression recycling apparatus

Info

Publication number
JPH05309726A
JPH05309726A JP2411335A JP41133590A JPH05309726A JP H05309726 A JPH05309726 A JP H05309726A JP 2411335 A JP2411335 A JP 2411335A JP 41133590 A JP41133590 A JP 41133590A JP H05309726 A JPH05309726 A JP H05309726A
Authority
JP
Japan
Prior art keywords
pressure
fluid
compressor
container
line
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
Application number
JP2411335A
Other languages
Japanese (ja)
Other versions
JP3153907B2 (en
Inventor
Hirokazu Yoshioka
弘料 吉岡
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP41133590A priority Critical patent/JP3153907B2/en
Publication of JPH05309726A publication Critical patent/JPH05309726A/en
Application granted granted Critical
Publication of JP3153907B2 publication Critical patent/JP3153907B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/1703Introducing an auxiliary fluid into the mould
    • B29C45/1732Control circuits therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/78Measuring, controlling or regulating
    • B29C49/783Measuring, controlling or regulating blowing pressure
    • B29C2049/7832Blowing with two or more pressure levels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/4284Means for recycling or reusing auxiliaries or materials, e.g. blowing fluids or energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/42Component parts, details or accessories; Auxiliary operations
    • B29C49/4284Means for recycling or reusing auxiliaries or materials, e.g. blowing fluids or energy
    • B29C49/42845Recycling or reusing of fluid, e.g. pressure
    • B29C49/42855Blowing fluids, e.g. reducing fluid consumption
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Fluid-Pressure Circuits (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To attempt adoption of a general automatic control method by reducing an installation cost by a method wherein a low pressure line which recoveres to neighbourhood pressure wherein inlet pressure of a compressor which is divided by a compression ratio is provided, and a suction line of one compressor is switched reciprocally from sucking of a high pressure line to sucking of a low pressure line. CONSTITUTION:Fluid compressed to injecting pressure into a molding piece in a die 7 with a compressor 3 is reserved in a compression fluid container 5 through a check valve 4, and the compressed fluid is injected into the molding piece in the die 7 by opening an injection valve 6. At a point of time when molding has been completed, a recovery valve 9 is opened and controlled with a compression sensor, a timer, etc., until an inside of a high pressure container 1 reaches equlibrium pressure. When it has reached equilibrium, an inlet valve 12 of a low pressure sucking pressure container 13 is opened, and the compression fluid is recovered until the container 13 reaches the equilibrium pressure. Beside, pressure of the high pressure container 1 is set to a specific pressure with a sensor 21, and low pressure fluid is supplied to the compressor 3 from the low pressure container 13. Then, it is compressed to at least the pressure set with the sensor 21 of the high pressure container 1 and supplied to the high pressure container 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は熱可塑性合成樹脂射出
成形における、中空成形品を作る際に、金型内の成形品
内部に送り込む圧縮流体を製造するための流体圧縮リサ
イクル装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fluid compression recycling apparatus for producing a compressed fluid to be fed into a molded product in a mold when making a hollow molded product in thermoplastic synthetic resin injection molding.

【0002】[0002]

【従来の技術】我が国における10Kg/cm2以上の圧縮流体
(但し空気は50Kg/cm2)は、高圧ガス取締法にしたがつ
て運用されねばならないことになつている。この法律に
よると、10Kg/cm2以上の圧縮ガスの製造装置の運転に携
わる人は、1日の製造量が100Nm3以上となると、丙種作
業主任者免許(試験合格後1年間高圧ガス製造装置の運
転経験を要す)が必要となるため、それ以下の規模の製
造装置の方が、ユ−ザにとつては使い易い。しかしなが
ら小容量、高吐出圧力の圧縮機は商業的設計ではモ−タ
駆動レシプロ式ガス圧縮機の分野で、200Kg/cm2までは
開発されてはいるものの、24時間連続運転の実績及び信
頼性がない。
2. Description of the Related Art A compressed fluid of 10 kg / cm 2 or more (however, air is 50 kg / cm 2 ) in Japan must be operated according to the High Pressure Gas Control Law. According to this law, a person engaged in the operation of a device for producing compressed gas of 10 kg / cm 2 or more, when the daily production amount becomes 100 Nm 3 or more, is licensed as a chief of species work (high pressure gas production device for one year after passing the test. Therefore, a manufacturing apparatus of a smaller scale is easier for a user to use. However, small capacity, high discharge pressure compressors are commercially designed in the field of motor-driven reciprocating gas compressors, and although they have been developed up to 200 Kg / cm 2, they have a proven record of 24 hours continuous operation and reliability. There is no.

【0003】この発明が目指している300Kg/cm2前後の
装置は大型となり、1日の製造量が100Nm3では納まら
ず、数倍の製造量となるため、上記のような丙種作業主
任者が必要となる。一方、ブ−スタ式圧縮機では、吸入
圧力が30〜50Kg/cm2となり、使用後の回収圧力を下げる
ために、2台の圧縮機a,bを使用している(図3参
照)。
The device of about 300 Kg / cm 2 aimed at by the present invention is large in size and the daily production amount cannot be set to 100 Nm 3 , which is several times the production amount. Will be needed. On the other hand, in the booster compressor, the suction pressure is 30 to 50 kg / cm 2 , and two compressors a and b are used to lower the recovery pressure after use (see FIG. 3).

【0004】この方法であると、個々の圧縮機で吐出す
る流体圧力が高圧流体となり、それぞれの吸入量の合計
が高圧流体の製造量となり、全体としては1/2の圧縮流
体量しか得られないことになる。また圧縮機が2台必要
となるため、製作費も2倍必要となる。一方、金型内の
成形品の形状や厚みにより注入ガス圧力は異なるので、
従来では金型内の成形品に流体を注入する直前に、圧力
調整弁を設置することにより、所定の圧力に調整後流体
を注入する方法等がある。
According to this method, the pressure of the fluid discharged by each compressor becomes a high-pressure fluid, and the sum of the respective suction amounts becomes the production amount of the high-pressure fluid, so that only a half of the compressed fluid amount can be obtained. There will be no. Also, since two compressors are required, the production cost will be doubled. On the other hand, since the injection gas pressure differs depending on the shape and thickness of the molded product in the mold,
Conventionally, there is a method of injecting the fluid after adjusting it to a predetermined pressure by installing a pressure adjusting valve immediately before injecting the fluid into the molded product in the mold.

【0005】[0005]

【発明が解決しようとする課題】この方法であると、圧
力調整弁の能力(圧力と流量特性)が、成形品に必要な
圧力と流量にマツチングする必要があり、また成形品が
変わる毎にセツトし直さねばならないが、自動化するた
めには装置が大型化しコストも高く付くという点に課題
が残されている。
With this method, it is necessary to match the capacity (pressure and flow rate characteristics) of the pressure regulating valve to the pressure and flow rate required for the molded product, and each time the molded product changes. Although it has to be reset, there remains a problem in that the size and cost of the device are high for automation.

【0006】[0006]

【課題を解決するための手段】ここにおいてこの発明は
圧縮機で圧縮された流体の使用後、回収リサイクルして
使用する時、回収ラインを回収して均圧になつた流体を
放出する装置において、回収流体ラインを圧縮機の吸入
圧力まで回収する高圧ラインと、均圧して残つた流体を
圧縮機の吸入圧力を圧縮比で除した近傍圧力まで回収す
る低圧ラインとに分け、一台の圧縮機の吸入ラインを、
高圧ラインの吸入と低圧ラインの吸入に適時切り替え、
低圧ラインの流体を高圧ライン圧力まで圧縮し、再使用
することにより回収ラインの圧力を下げ、放出するガス
の圧力を圧縮機の吸入圧力の圧縮比で除した圧力近傍ま
で下げることを特徴とする流体圧縮リサイクル装置を提
案するものである。
According to the present invention, there is provided an apparatus for recovering a recovery line after use of a fluid compressed by a compressor to recover and recycle the fluid, and discharging the fluid having a pressure equalized. , A high-pressure line that collects the collected fluid line up to the suction pressure of the compressor and a low-pressure line that collects the remaining fluid after pressure equalization to a pressure near the pressure obtained by dividing the suction pressure of the compressor by the compression ratio. The suction line of the machine
Timely switching between high pressure line intake and low pressure line intake,
It is characterized in that the fluid in the low-pressure line is compressed to the pressure in the high-pressure line and reused to lower the pressure in the recovery line, and the pressure of the gas to be discharged is reduced to near the pressure obtained by dividing the pressure of the gas discharged by the compression ratio of the compressor suction pressure A fluid compression recycling device is proposed.

【0007】[0007]

【実施例】以下に図1に示した実施例に基づいてこの発
明を詳しく説明する。これは8.5Kg/cm2から300Kg/cm2
昇圧する例である。高圧吸入圧力容器1により吸入流体
出口弁2を通つて、高圧の吸入流体は圧縮機3に供給さ
れる。この時逆止弁14により低圧吸入圧力容器13への逆
流はない。この圧縮機3で金型7内の成形品への注入圧
力まで圧縮された圧縮流体は、逆止弁4を通つて圧縮流
体容器5に溜められ、圧縮流体注入弁6を開いて前記圧
縮流体を金型7内の成形品内に注入する。この時、金型
7の入口の圧力流体注入ライン内に設けられた圧力セン
サ8の設定圧力により、開閉時間をコントロ−ルされ、
成形品内の流体圧力が所定の圧力になるようにコントロ
−ルされる。
The present invention will be described in detail below with reference to the embodiment shown in FIG. This is an example of boosting from 8.5 kg / cm 2 to 300 Kg / cm 2. The high-pressure suction fluid is supplied to the compressor 3 by the high-pressure suction pressure container 1 through the suction fluid outlet valve 2. At this time, there is no backflow to the low pressure suction pressure vessel 13 due to the check valve 14. The compressed fluid compressed by the compressor 3 up to the injection pressure into the molded product in the mold 7 is accumulated in the compressed fluid container 5 through the check valve 4, and the compressed fluid injection valve 6 is opened to open the compressed fluid. Is injected into the molded product in the mold 7. At this time, the opening and closing time is controlled by the set pressure of the pressure sensor 8 provided in the pressure fluid injection line at the inlet of the mold 7.
The fluid pressure in the molded product is controlled to a predetermined pressure.

【0008】次に成形品内の流体圧力は所定の時間保持
され、成形品の成形が完了した時点で圧縮流体は回収弁
9を開いて、高圧吸入圧力容器1内が平衡圧に達するま
で、圧力センサ又はタイマ等で、回収弁9は制御され、
平衡圧力に達したならば、低圧吸入圧力容器13の入口弁
12を開いて、低圧吸入圧力容器13が平衡圧力に達するま
で回収される。平衡圧力に達したならば、低圧吸入圧力
容器13の入口弁12は閉められる。この時、逆止弁11によ
り回収ラインの高圧系流体は逆流しない。
Next, the fluid pressure in the molded product is maintained for a predetermined time, and when the molding of the molded product is completed, the compressed fluid opens the recovery valve 9 until the inside of the high-pressure suction pressure container 1 reaches the equilibrium pressure. The recovery valve 9 is controlled by a pressure sensor or a timer,
Once the equilibrium pressure is reached, the inlet valve of the low pressure suction pressure vessel 13
Open 12 and collect until low pressure inlet pressure vessel 13 reaches equilibrium pressure. Once the equilibrium pressure is reached, the inlet valve 12 of the low pressure suction pressure vessel 13 is closed. At this time, the check valve 11 prevents the high-pressure system fluid in the recovery line from flowing backward.

【0009】次に回収弁9を閉じ、大気放出弁10を開い
て金型7内の成形品内流体圧力を大気圧まで下げた後、
大気放出弁10を閉じ、金型7内から成形品を取り出す。
一方、高圧吸入圧力容器1の圧力は、センサ21で所定の
圧力をセツトし、それ以下の場合は吸入流体出口弁2を
閉じ、低圧吸入圧力容器13から、低圧吸入流体を圧縮機
3に供給し、圧縮機3で高圧吸入圧力容器13のセンサ21
のセツト圧力以上まで圧縮し、高圧吸入圧力供給弁15を
開いて、高圧吸入圧力容器1に供給し、前記センサ21の
セツト圧力に達したならば、高圧吸入圧力供給弁15を閉
じ、再び吸入流体出口弁2を開いて、同じサイクルを繰
り返えす。他方、低圧吸入圧力容器13のセンサ22は、ブ
−スタ3への供給圧力にセツトされ、セツト圧以下にな
ると、流体としてのN2供給弁19が開いて、N2ボンベ17
出口の圧力調整弁18で、所定の圧力にコントロ−ルされ
たN2が、自動的に供給される。その供給量は、大気に
放出されたガス量に等しくなる。
Next, after the recovery valve 9 is closed and the atmospheric release valve 10 is opened to reduce the fluid pressure in the molded product in the mold 7 to the atmospheric pressure,
The atmosphere release valve 10 is closed and the molded product is taken out of the mold 7.
On the other hand, the pressure of the high-pressure suction pressure vessel 1 is set to a predetermined pressure by the sensor 21, and if it is lower than that, the suction fluid outlet valve 2 is closed and the low-pressure suction pressure vessel 13 supplies the low-pressure suction fluid to the compressor 3. The compressor 21 uses the sensor 21 of the high-pressure suction pressure container 13
Compressed to a pressure higher than the set pressure, the high pressure suction pressure supply valve 15 is opened to supply to the high pressure suction pressure vessel 1, and when the set pressure of the sensor 21 is reached, the high pressure suction pressure supply valve 15 is closed and suction is performed again. Open fluid outlet valve 2 and repeat the same cycle. On the other hand, the sensor 22 of the low-pressure suction pressure container 13 is set to the supply pressure to the booster 3, and when the pressure becomes lower than the set pressure, the N 2 supply valve 19 as a fluid opens and the N 2 cylinder 17
The pressure adjusting valve 18 at the outlet automatically supplies N 2 controlled to a predetermined pressure. The amount supplied is equal to the amount of gas released to the atmosphere.

【0010】また大気放出圧力を下げ、N2を有効に使
用する方法として、第2図に示すように大気放出弁10の
先きに、成形品の注入流体量の10倍程度のアキユムレ−
タ23を設け、大気放出弁10とアキユムレ-タ23の間に、
バイパス回路24を設け、回収タンク13の入口に接続す
る。バイパス回路24には、バイパス弁22を設け、回収タ
ンク13への低圧回収ラインの回収が完了した後、回収弁
9及び低圧吸入圧力容器13の入口弁12を閉じ、大気放出
弁10を開いて、残ガスをアキユムレ−タに通し、圧力を
1/10に減圧した後、大気放出弁10を閉じ、バイパス弁22
を開いて、油圧ポンプ25から、低圧吸入圧力容器の圧力
以上10Kg/cm2以下(高圧流体にならないため)の油圧を
送り、アキユムレ−タ23内の圧力を圧縮し、プレツシヤ
スイツチ26が所定の圧力に達すると、バイパス弁22を閉
じる。油圧ポンプ25を停止し、アキユムレ−タ23の油を
油タンク内に落して、次回のサイクルに備える。この方
法によると、圧縮するN2は、10Kg/cm2以下の圧力であ
るため、高圧ガス取締法に適用外であるので、自由かつ
安価に製作でき、しかもN2の回収率が高くなり、ラン
ニングコストの一層の低減を計ることができる。
Further, as a method of lowering the atmospheric discharge pressure and effectively using N 2 , as shown in FIG. 2, before the atmospheric discharge valve 10, about 10 times the injected fluid amount of the molded product is used.
23 is provided, and between the atmospheric release valve 10 and the Aki Yum Leta 23,
A bypass circuit 24 is provided and connected to the inlet of the recovery tank 13. A bypass valve 22 is provided in the bypass circuit 24, and after the recovery of the low-pressure recovery line to the recovery tank 13 is completed, the recovery valve 9 and the inlet valve 12 of the low-pressure suction pressure container 13 are closed, and the atmosphere release valve 10 is opened. , Pass the residual gas through the accumulator and apply pressure.
After reducing the pressure to 1/10, the atmospheric release valve 10 was closed and the bypass valve 22
Open and send the hydraulic pressure above the pressure of the low pressure suction pressure container to 10 kg / cm 2 or less (because it does not become a high pressure fluid) from the hydraulic pump 25 to compress the pressure in the accumulator 23, and the pressure switch 26 When the predetermined pressure is reached, the bypass valve 22 is closed. The hydraulic pump 25 is stopped and the oil of the accumulator 23 is dropped into the oil tank to prepare for the next cycle. According to this method, N 2 to be compressed has a pressure of 10 Kg / cm 2 or less, and is not applicable to the high-pressure gas control method. Therefore, it can be manufactured freely and inexpensively, and the recovery rate of N 2 is high. The running cost can be further reduced.

【0011】[0011]

【発明の効果】この発明によれば次のような効果が得ら
れる。すなわち、 1)ブ−スタ式圧縮機では、圧縮比が6前後が一般的
で、300Kg/cm2まで上げるには吸入圧が50Kg/cm2程度と
なり、大気放出圧力を下げるにはさらに低圧側に圧縮機
を一台設置し、8.5Kg/cm2から51Kg/cm2程度に圧縮し、
高圧吸入ラインに供給する方法を取るため、2台の圧縮
機が必要となり、1台設備するには200万程度の費用が
必要となり、また吐出圧力が51Kg/cm2となると、高圧流
体製造設備となり、製造量が2倍となるため、丙種作業
主任者が1直に1人、3交代勤務では、3人+1人の代
勤者が必要となるので、丙種作業主任者が居ない場合
は、1/2の製造量の圧縮機しか設置できないが、この発
明の装置では、設置圧縮機の製造量の(1−1/6)X100
%=83%まで使用できるので、実質的に問題にならない。
また圧縮機が一台で済むので、設備費が安く付く。
According to the present invention, the following effects can be obtained. That is, 1) blanking - the static type compressor, longitudinal compression ratio is 6 common, suction pressure to raise up to 300 Kg / cm 2 becomes 50 Kg / cm 2 or so, further low-pressure side to decrease the atmospheric discharge pressure the compressor was installed single, compressed from 8.5 kg / cm 2 to about 51 kg / cm 2, the
Since it uses a method of supplying to the high-pressure suction line, it requires two compressors, one unit requires about 2 million costs, and when the discharge pressure becomes 51 Kg / cm 2 , high-pressure fluid manufacturing equipment Since the production amount will be doubled, one person will work as a chief of class work at one shift and three shift workers will require 3 + 1 people, so if there is no chief of class work. , Only 1/2 the production amount of the compressor can be installed, but with the device of the present invention, the production amount of the installed compressor is (1-1 / 6) X100.
Since it can be used up to% = 83%, there is practically no problem.
Since only one compressor is required, equipment costs are low.

【0012】2)金型内の成形品に適した圧力を供給す
る圧力を、センサ(毎秒20回程度のサンプリング可能な
もの)で成形品内の上昇圧力を検出し、そのセツト圧力
で弁を開閉するという一般的な自動制御方法で済むの
で、費用が安価と成り装置も小型化する。
2) A sensor (a device capable of sampling about 20 times per second) detects the rising pressure in the molded product, and the set pressure is used to operate the valve. Since the general automatic control method of opening and closing is sufficient, the cost is low and the device is downsized.

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

【図1】この発明の一実施例の構成図である。FIG. 1 is a configuration diagram of an embodiment of the present invention.

【図2】一部分の変更例を示す構成図である。FIG. 2 is a configuration diagram showing a modification example of a part.

【図3】従来例の略図である。FIG. 3 is a schematic view of a conventional example.

【符号の説明】[Explanation of symbols]

1 高圧吸入圧力容器 3 圧縮機 8 圧力センサ 9 回収弁 10 低圧吸入圧力容器 1 High-pressure suction pressure vessel 3 Compressor 8 Pressure sensor 9 Recovery valve 10 Low-pressure suction pressure vessel

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】圧縮機で圧縮された流体の使用後、回収リ
サイクルして使用する時、回収ラインを回収して均圧に
なつた流体を放出する装置において、回収流体ラインを
圧縮機の吸入圧力まで回収する高圧ラインと、均圧して
残つた流体を圧縮機の吸入圧力を圧縮比で除した近傍圧
力まで回収する低圧ラインとに分け、一台の圧縮機の吸
入ラインを、高圧ラインの吸入と低圧ラインの吸入に適
時切り替え、低圧ラインの流体を高圧ライン圧力まで圧
縮し、再使用することにより回収ラインの圧力を下げ、
放出するガスの圧力を圧縮機の吸入圧力の圧縮比で除し
た圧力近傍まで下げることを特徴とする流体圧縮リサイ
クル装置。
Claim: What is claimed is: 1. When a fluid compressed by a compressor is used for recovery and recycling after use, in a device for recovering the recovery line and discharging the fluid having a pressure equalized, the recovery fluid line is sucked by the compressor. Separate the high-pressure line to recover the pressure and the low-pressure line to recover the fluid remaining after the equalization until the pressure near the pressure obtained by dividing the suction pressure of the compressor by the compression ratio. Timely switching between suction and low-pressure line suction, compressing the low-pressure line fluid to the high-pressure line pressure and reusing it to lower the recovery line pressure,
A fluid compression recycle device characterized in that the pressure of the gas to be released is reduced to near the pressure obtained by dividing the suction pressure of the compressor by the compression ratio.
JP41133590A 1990-12-18 1990-12-18 Gas compression recycling equipment Expired - Fee Related JP3153907B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP41133590A JP3153907B2 (en) 1990-12-18 1990-12-18 Gas compression recycling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP41133590A JP3153907B2 (en) 1990-12-18 1990-12-18 Gas compression recycling equipment

Publications (2)

Publication Number Publication Date
JPH05309726A true JPH05309726A (en) 1993-11-22
JP3153907B2 JP3153907B2 (en) 2001-04-09

Family

ID=18520353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP41133590A Expired - Fee Related JP3153907B2 (en) 1990-12-18 1990-12-18 Gas compression recycling equipment

Country Status (1)

Country Link
JP (1) JP3153907B2 (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0655314A1 (en) * 1993-11-26 1995-05-31 KRUPP CORPOPLAST MASCHINENBAU GmbH Multiple use of compressed air
EP0824978A1 (en) * 1996-08-19 1998-02-25 Thomassen & Drijver-Verblifa N.V. Device for remodelling a hollow object
FR2827541A1 (en) * 2001-07-20 2003-01-24 Technoplan Engineering S A Container blower, especially for making plastic bottles from preforms, has gas recuperation system with chamber and valve
WO2006029584A1 (en) * 2004-09-14 2006-03-23 Sig Technology Ltd Method and device for blow forming containers
JP2007530314A (en) * 2004-03-25 2007-11-01 クロネス・アクチェンゲゼルシャフト Hollow body manufacturing method and apparatus for reducing air consumption
FR2902366A1 (en) * 2007-05-14 2007-12-21 Dixi Proc Producing hollow plastic articles by blow molding comprises recovering injected gas and compressing the recovered gas for use in a subsequent inflation step
KR100870057B1 (en) * 2007-03-14 2008-11-24 한국에너지기술연구원 recycle method of cooling gas using the recycle device for cooling gas
JP2009506906A (en) * 2005-09-08 2009-02-19 クロネス・アクチェンゲゼルシャフト Method and apparatus for controlling and adjusting a hollow body production unit
WO2011110149A3 (en) * 2010-03-08 2012-01-12 Khs Corpoplast Gmbh Method and device for blow -forming containers
JP2012081714A (en) * 2010-10-14 2012-04-26 Nissei Asb Mach Co Ltd Method of operating blow molding apparatus
JP2012523971A (en) * 2009-04-16 2012-10-11 カーハーエス コーポプラスト ゲーエムベーハー Method and apparatus for blow molding containers
WO2015004109A1 (en) * 2013-07-09 2015-01-15 Sidel Participations Method for forming containers comprising steps of recycling the blow-moulding fluid by means of a vessel
CN111761805A (en) * 2020-07-16 2020-10-13 苏州同大机械有限公司 Pulsating cooling blowing device of blow molding machine and blowing method thereof

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0655314A1 (en) * 1993-11-26 1995-05-31 KRUPP CORPOPLAST MASCHINENBAU GmbH Multiple use of compressed air
EP0824978A1 (en) * 1996-08-19 1998-02-25 Thomassen & Drijver-Verblifa N.V. Device for remodelling a hollow object
NL1003827C2 (en) * 1996-08-19 1998-02-26 Thomassen & Drijver Device for remodeling a hollow metal object.
US5895666A (en) * 1996-08-19 1999-04-20 Thomassen & Drijver-Verblifa B.V. Device for remodelling a hollow object
FR2827541A1 (en) * 2001-07-20 2003-01-24 Technoplan Engineering S A Container blower, especially for making plastic bottles from preforms, has gas recuperation system with chamber and valve
WO2003009993A1 (en) * 2001-07-20 2003-02-06 Technoplan Engineering S.A. Container blowing device
US7320586B2 (en) 2001-07-20 2008-01-22 Technoplan Engineering S.A. Container blowing device
US7892477B2 (en) 2004-03-25 2011-02-22 Krones Ag Process and device for the manufacture of a particularly heat-resistant hollow body
JP2007530314A (en) * 2004-03-25 2007-11-01 クロネス・アクチェンゲゼルシャフト Hollow body manufacturing method and apparatus for reducing air consumption
US9044892B2 (en) 2004-03-25 2015-06-02 Krones Ag Process and device for the manufacture of a particularly heat-resistant hollow body
US8550805B2 (en) 2004-03-25 2013-10-08 Krones Ag Process and device for the manufacture of a particularly heat-resistant hollow body
WO2006029584A1 (en) * 2004-09-14 2006-03-23 Sig Technology Ltd Method and device for blow forming containers
US7790097B2 (en) 2004-09-14 2010-09-07 Khs Corpoplast Gmbh & Co. Kg Method and device for blow forming containers
JP2009506906A (en) * 2005-09-08 2009-02-19 クロネス・アクチェンゲゼルシャフト Method and apparatus for controlling and adjusting a hollow body production unit
KR100870057B1 (en) * 2007-03-14 2008-11-24 한국에너지기술연구원 recycle method of cooling gas using the recycle device for cooling gas
EP2014443A1 (en) * 2007-05-14 2009-01-14 Dixi Processing Method for manufacturing hollow plastic bodies by blowing, device and installation for implementing same
FR2902366A1 (en) * 2007-05-14 2007-12-21 Dixi Proc Producing hollow plastic articles by blow molding comprises recovering injected gas and compressing the recovered gas for use in a subsequent inflation step
JP2012523971A (en) * 2009-04-16 2012-10-11 カーハーエス コーポプラスト ゲーエムベーハー Method and apparatus for blow molding containers
WO2011110149A3 (en) * 2010-03-08 2012-01-12 Khs Corpoplast Gmbh Method and device for blow -forming containers
JP2012081714A (en) * 2010-10-14 2012-04-26 Nissei Asb Mach Co Ltd Method of operating blow molding apparatus
WO2015004109A1 (en) * 2013-07-09 2015-01-15 Sidel Participations Method for forming containers comprising steps of recycling the blow-moulding fluid by means of a vessel
FR3008337A1 (en) * 2013-07-09 2015-01-16 Sidel Participations "PROCESS FOR FORMING CONTAINERS COMPRISING RECYCLING STAGES OF THE BLOWING FLUID USING A RESERVOIR, PRESSURE IN THE OSCILLATING RESERVOIR BETWEEN A STORAGE PRESSURE AND A CLEARING PRESSURE"
CN111761805A (en) * 2020-07-16 2020-10-13 苏州同大机械有限公司 Pulsating cooling blowing device of blow molding machine and blowing method thereof
CN111761805B (en) * 2020-07-16 2021-11-05 苏州同大机械有限公司 Pulsating cooling blowing device of blow molding machine and blowing method thereof

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