JPS5892441A - Method for controlling automatic winding-up of filter material in air filter - Google Patents
Method for controlling automatic winding-up of filter material in air filterInfo
- Publication number
- JPS5892441A JPS5892441A JP19137081A JP19137081A JPS5892441A JP S5892441 A JPS5892441 A JP S5892441A JP 19137081 A JP19137081 A JP 19137081A JP 19137081 A JP19137081 A JP 19137081A JP S5892441 A JPS5892441 A JP S5892441A
- Authority
- JP
- Japan
- Prior art keywords
- air
- filter
- filter material
- signal
- value
- 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.)
- Pending
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は漸次巻取られるロール状の濾材を用いて空気中
の塵を濾過捕集する空調用エアーフィルターにおける濾
材自動巻取9制御方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for automatically winding up a filter medium 9 in an air conditioning air filter that filters and collects dust in the air using a roll-shaped filter medium that is gradually wound up.
従来、この種の濾材自動巻取り制御方法としては差圧検
出方式とタイマー設定方式とがある。その前者の差圧検
出方式は濾過捕集した塵による濾材の目詰り度合を差圧
検知器により検知して濾材の巻取りを行なう方法であり
、この場合、差圧検知器の適当な設置個所がなり、シか
も空調機の能力上一般には差圧の変化がわずかなので、
差圧検知器で正確に目詰り度合を検知して巻取も制御す
るξとが困−であって信頼性がなく、不適確なものであ
った。一方後者のタイマー設定方式は、タイマーにより
予め設定した一定時間毎に濾材の巻取りを行なう方法で
あり、Cの場合、エアーフィルターへの送風量が常に一
定していれば高精度でもって適確な濾材巻取りができる
が、しかしながら空調システムでは送風量を常に一定に
保っておくことは少なく、一般には設定量に応じて送風
機等の風量制御を行なって電力消費の節減をはかること
などから、送風量がたえず変化する場合が多い。このた
めにタイマーにより濾材巻取り時期を一定間隔に定めて
おくと、単位時間あた9の送風量が多い時期1r−は、
濾材の目詰りの進み度合が早くタイマーの設定時間がく
る前に圧力損失が所定以上番こ高くなってしまい、これ
Kて濾過効率が層くなるとともに、送風機の動力費アッ
プを招いてしまう問題が生じ、逆に単位時間あだ轢の送
風量が少ない時期には、濾材の目詰りの進み度合が遅い
ことから、圧力損失の低い使用可能状態にあるにもかか
わらずタイマー設定時間がきて巻取られてしまうといっ
た具合に、濾材の無駄な消費が余儀なくされて使用効率
が悪く不経済であるなどの間顯があった。Conventionally, this type of filter medium automatic winding control method includes a differential pressure detection method and a timer setting method. The former differential pressure detection method is a method in which a differential pressure detector detects the degree of clogging of the filter medium due to collected dust and winds up the filter medium.In this case, the differential pressure detector is installed at an appropriate location. Due to the capacity of the air conditioner, changes in differential pressure are generally small, so
It is difficult to accurately detect the degree of clogging with a differential pressure detector and control the winding, and it is unreliable and inaccurate. On the other hand, the latter timer setting method is a method in which the filter material is wound up at preset intervals using a timer. However, in air conditioning systems, the amount of air blown is rarely kept constant, and generally the air amount of a blower or other device is controlled according to the set amount in order to reduce power consumption. Air flow rate often changes constantly. For this purpose, if the time for winding the filter media is set at regular intervals using a timer, during the period 1r- when the amount of air blown per unit time is high,
The problem is that the filter media becomes clogged so quickly that the pressure loss becomes higher than the predetermined level before the timer set time is reached, which reduces the filtration efficiency and increases the power cost of the blower. On the other hand, when the amount of air blowing per unit time is low, the rate of clogging of the filter medium is slow, so even though the filter is in a usable state with low pressure loss, the timer setting time is reached and the filter is There was a problem that the filter media was used wastefully, resulting in poor usage efficiency and being uneconomical.
本発明の方法は、上記事情に鑑みなされたもので、従来
の差圧検知方式やタイマー設定方式と全く異なり、常に
適確な濾材自動看取り制御ができて、濾過効率を高め得
るとともに、濾材の無駄をナクシて該濾材の使用効率の
大幅なアップをはかることを目的としたものであり、ロ
ール状の濾材を用いたエアーフィルターに送風する送風
システムの風量信号と送風する被処理空気の含塵濃度信
号とを取出し、その風量信号及び濃度信号を演算器等で
積分していき、その値が濾材の濾過許容総風量設定値に
達した時に看取り機を動作させて濾材の一定量の巻取ゆ
を行なう方法を特徴とするものである。The method of the present invention has been developed in view of the above circumstances, and is completely different from the conventional differential pressure detection method and timer setting method. The purpose is to eliminate waste and significantly increase the efficiency of using the filter media, and it uses the air volume signal of the air blowing system that blows air to the air filter using the roll-shaped filter media and the dust content of the air being blown to be treated. The concentration signal is taken out, and the air volume signal and the concentration signal are integrated by a calculator, etc., and when the value reaches the set value of the total permissible air volume for filtering, the end-of-life monitoring machine is operated to wind up a certain amount of the filter material. It is characterized by a method of performing Yu.
以下本発明の方法を図面に基づいて説明する。The method of the present invention will be explained below based on the drawings.
181図は本発明の方法を実施する基本的装置の概略ブ
ロック図であり、送風システムの風量信号を風量信号送
出器1で取出し、又、被処理空気の含塵濃度信号を濃度
信号送出器2で取出し、その風量信号と濃度信号とを演
算処理器うで積分処理して、その値が濾材の濾過許容総
風量設定値に達したら、濾材巻取り機嶋を動作させて図
示しない濾材の一定量の巻取りを一回行なう。そして、
その−回の濾材巻取9後再び風量信号送出器1及び濃度
信号送出器2からの風量信号及び濃度信号を演算処理器
うで積分して、前記同様に濾材の巻取りを繰返し行なう
。FIG. 181 is a schematic block diagram of the basic equipment for carrying out the method of the present invention, in which the air volume signal of the ventilation system is taken out by the air volume signal transmitter 1, and the dust concentration signal of the air to be treated is taken out by the concentration signal transmitter 2. The air volume signal and concentration signal are integrally processed by an arithmetic processor, and when the value reaches the filtration permissible total air volume setting value of the filter media, the filter media winding machine is operated to maintain a constant flow rate of the filter media (not shown). Take up the amount once. and,
After winding up the filter medium 9, the air volume signal and concentration signal from the air volume signal transmitter 1 and the concentration signal transmitter 2 are again integrated by the arithmetic processor, and the winding of the filter medium is repeated in the same manner as described above.
第2図は前記の本発明の方法を実施する装置の具体的な
構成を示す一例のブロック図であり、送風システムの送
風機からの風量を風量制御信号送出器11によやζ−2
0mAの風量制御信号として取出し、又、送風システム
の送風機から送風される被処理空気の含塵濃度を重量式
含塵濃度計12y−より14−20mAの濃度信号とし
て取出し、その両者の信号出力をA−D変換器15ムで
アナログからデジタルに変換して、その信号でパルスを
分周I11うBで演算してカウンター15Cに送り、+
のカウンターBeでパルス数をカウント(歩進信号動作
)即ち積分処理する。その後、その値が濾材の濾過許容
総風量設定値に達したら、浦材巻取り機14を動作させ
て図示しない濾材の一定量の巻取りを一回行なう。そし
て、その−回の濾材看取りが終了した後1巻取轢機麹に
よ轢前記カウンター15cに巻取り終了信号をフィード
バックし、これにて再度前記と同様な積分処理を開始し
て、その値が設定値に達した都度繰返し濾材巻取吟を行
なう。又。FIG. 2 is a block diagram of an example showing a specific configuration of an apparatus for implementing the method of the present invention, in which the air volume from the blower of the air blowing system is controlled by the air volume control signal transmitter 11 and ζ-2.
A 0 mA airflow control signal is taken out, and a 14-20 mA concentration signal is taken out from the gravimetric dust concentration meter 12y, and the dust concentration of the air to be treated is blown from the blower of the blowing system. Convert from analog to digital with A-D converter 15, calculate the pulse with frequency division I11B, and send it to counter 15C, +
The counter Be counts the number of pulses (stepping signal operation), that is, performs integration processing. Thereafter, when the value reaches the set value of the total permissible air volume for filtering the filter medium, the ura material winding machine 14 is operated to wind up a certain amount of the filter medium (not shown) once. Then, after the end of the filter medium inspection is completed, a winding completion signal is fed back to the counter 15c by the first winding machine koji, and the same integral process as described above is started again, and the value is The filter material is wound up repeatedly each time the value reaches the set value. or.
−回毎の濾材看取り信号を信号表示器15に送って濾材
巻終り及び過負荷等の信号表示を行なう。- A filter medium end signal is sent every time to the signal display 15 to display signals such as the end of filter medium winding and overload.
本発明の方法は9以上説明した如くなしたため従来の差
圧検知方式やタイマー設定方式と全く異なり、常に適確
な濾材自動看取り制御が可能で。Since the method of the present invention is performed as explained above, it is completely different from the conventional differential pressure detection method and timer setting method, and allows accurate automatic end-of-life control of the filter medium at all times.
濾過効率の向上がはかれるとともに、濾材の無駄をなく
して濾材の使用効率を大幅にアップでき。In addition to improving filtration efficiency, it also eliminates waste of filter media and greatly increases the efficiency of filter media usage.
かつ送風機の動力費等の運転経費の節減がはかれる。又
、被処理空気の含塵濃度の信号を取出すので、空気中の
含塵の割合に応してフィルターを制御でき、フィルター
の使用効率がさらに向上することとなる。In addition, operating costs such as power costs for blowers can be reduced. Furthermore, since a signal of the dust concentration of the air to be treated is extracted, the filter can be controlled according to the proportion of dust in the air, further improving the efficiency of use of the filter.
第1図は本発明の方法を実施する装置の概要ブロック図
、第2図は同装置の具体的構成を示すブロック図である
。
1・・・風量信号送出器、2・・・含塵濃度送出器、う
・・・演算処理器
特許出願人
トiり自動車工業株式会社
代表1ii11田俊夫FIG. 1 is a schematic block diagram of an apparatus for implementing the method of the present invention, and FIG. 2 is a block diagram showing a specific configuration of the apparatus. 1... Air volume signal transmitter, 2... Dust concentration transmitter, U... Arithmetic processor Patent applicant Tori Jidosha Kogyo Co., Ltd. Representative 1ii11 Toshio Ta
Claims (1)
送風システムの風量信号と送風する被処理空気の含塵濃
度信号とを取出し、その風量信号及び濃度信号を積分し
ていき、その値が濾材の濾過許容総風量設定値に達した
時に巻取り機を動作させて濾材の一定量の巻取りを行な
うことを特徴とするエアーフィルターにおける濾材自動
巻取り制御方法Air filter using roll-shaped filter media Kpm The air volume signal of the air blowing system and the dust concentration signal of the air to be blown are taken out, the air volume signal and the concentration signal are integrated, and the value is the value of the filter media. A method for automatically winding up a filter medium in an air filter, which comprises operating a winding machine to wind up a certain amount of the filter medium when the total permissible air volume for filtration reaches a set value.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19137081A JPS5892441A (en) | 1981-11-27 | 1981-11-27 | Method for controlling automatic winding-up of filter material in air filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19137081A JPS5892441A (en) | 1981-11-27 | 1981-11-27 | Method for controlling automatic winding-up of filter material in air filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5892441A true JPS5892441A (en) | 1983-06-01 |
Family
ID=16273454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19137081A Pending JPS5892441A (en) | 1981-11-27 | 1981-11-27 | Method for controlling automatic winding-up of filter material in air filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5892441A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5071926A (en) * | 1973-11-09 | 1975-06-14 | ||
| JPS5129525A (en) * | 1974-09-04 | 1976-03-12 | Kanebo Ltd | NANNENAKURIRUKEISENINOSEIZOHO |
| JPS5390394A (en) * | 1977-01-19 | 1978-08-09 | Bayer Ag | Process for producing copolymer acrylonitrile and vinyl chloride |
-
1981
- 1981-11-27 JP JP19137081A patent/JPS5892441A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5071926A (en) * | 1973-11-09 | 1975-06-14 | ||
| JPS5129525A (en) * | 1974-09-04 | 1976-03-12 | Kanebo Ltd | NANNENAKURIRUKEISENINOSEIZOHO |
| JPS5390394A (en) * | 1977-01-19 | 1978-08-09 | Bayer Ag | Process for producing copolymer acrylonitrile and vinyl chloride |
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