JP3002683B2 - Photosensitive material processing equipment - Google Patents
Photosensitive material processing equipmentInfo
- Publication number
- JP3002683B2 JP3002683B2 JP2060606A JP6060690A JP3002683B2 JP 3002683 B2 JP3002683 B2 JP 3002683B2 JP 2060606 A JP2060606 A JP 2060606A JP 6060690 A JP6060690 A JP 6060690A JP 3002683 B2 JP3002683 B2 JP 3002683B2
- Authority
- JP
- Japan
- Prior art keywords
- photosensitive material
- drying
- processing
- section
- infrared
- 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 - Fee Related
Links
- 239000000463 material Substances 0.000 title claims description 142
- 238000012545 processing Methods 0.000 title claims description 78
- 238000001035 drying Methods 0.000 claims description 118
- 238000007603 infrared drying Methods 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 23
- 238000007602 hot air drying Methods 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 13
- 241000519995 Stachys sylvatica Species 0.000 claims description 7
- 230000003247 decreasing effect Effects 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 3
- 230000032258 transport Effects 0.000 description 37
- 238000012546 transfer Methods 0.000 description 13
- 230000000052 comparative effect Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000000839 emulsion Substances 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- 238000003780 insertion Methods 0.000 description 6
- 230000037431 insertion Effects 0.000 description 6
- 238000003756 stirring Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000009529 body temperature measurement Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 108010010803 Gelatin Proteins 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 230000007723 transport mechanism Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000007601 warm air drying Methods 0.000 description 1
Landscapes
- Photographic Processing Devices Using Wet Methods (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は感光材料処理装置に関し、詳しくは処理液
で処理した感光材料を乾燥する乾燥部を有する感光材料
処理装置に関する。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a photosensitive material processing apparatus, and more particularly, to a photosensitive material processing apparatus having a drying section for drying a photosensitive material processed with a processing solution.
[従来の技術] 露光済の感光材料を処理する感光材料処理装置では、
例えば感光材料を現像、定着、水洗し、この処理された
感光材料を、感光部で搬送しながら乾燥するものがあ
る。[Prior art] In a photosensitive material processing apparatus for processing an exposed photosensitive material,
For example, there is a type in which a photosensitive material is developed, fixed, washed with water, and the processed photosensitive material is dried while being conveyed in a photosensitive section.
この感光材料の乾燥として、温風を感光材料に当て乾
燥する温風乾燥方式と、赤外線を照射して乾燥する赤外
線乾燥方式とがあるが、この乾燥はその仕上り画質の向
上、処理量の増加、エネルギー消費の削減、装置の簡
易、小型等を図る上で重要な要因となっている。There are two types of drying of the photosensitive material: a hot air drying method in which hot air is applied to the photosensitive material for drying, and an infrared drying method in which infrared light is applied for drying. This drying improves the finished image quality and increases the processing amount. This is an important factor in reducing energy consumption and simplifying and miniaturizing the device.
[発明が解決しようとする課題] ところで、温風乾燥方式は、ソフトな乾燥ができ乾燥
ムラがなく、感光材料の仕上り画質が良好であるが、乾
燥に時間がかかる。このため、乾燥部の搬送距離を長く
したり、ヒータ容量を大きくすることが考えられるが、
装置が大型化し、エネルギーコストも増大することにな
る。[Problems to be Solved by the Invention] In the hot air drying method, soft drying is possible without drying unevenness, and the finished image quality of the photosensitive material is good, but drying takes time. For this reason, it is conceivable to lengthen the transport distance of the drying unit or increase the heater capacity.
The equipment becomes larger and the energy cost increases.
また、赤外線乾燥方式は乾燥温度を高くすることがで
き、乾燥能力が向上するが、感光材料の黒化部と白抜け
部とで残留水分に差が生じたり、乾燥を十分に行なうよ
うにした場合には黒化部または白抜け部のゼラチン層が
先に硬化してギラ付くようになり、画質低下が生じ易
い。In addition, the infrared drying method can increase the drying temperature and improve the drying ability. However, there is a difference in the residual moisture between the blackened portion and the blank portion of the photosensitive material, or the drying is sufficiently performed. In such a case, the gelatin layer in the blackened portion or the white spot is hardened first and becomes glaring, and the image quality tends to be deteriorated.
そこで、この発明者らはフィルムの乾燥について種々
研究した結果、乾燥時間の経過によって、感光材料を残
留水分率と表面温度が変化し、これより第1図に示すよ
うな感光材料乾燥曲線を求めることができた。The inventors of the present invention have conducted various studies on the drying of the film. As a result, the moisture content of the photosensitive material and the surface temperature of the photosensitive material change with the elapse of the drying time. From this, a photosensitive material drying curve as shown in FIG. 1 is obtained. I was able to.
第1図中の実線は、乾燥時間の経過と共に感光材料の
残留水分率が変化しておく様子を示しており、左の縦軸
と実線の交点は乾燥時間=0であるので、感光材料残留
水分率は100%である。The solid line in FIG. 1 shows how the residual moisture content of the photosensitive material changes with the elapse of the drying time. Since the intersection of the left vertical axis and the solid line is the drying time = 0, the remaining photosensitive material remains unchanged. Moisture content is 100%.
第1図中破線は、乾燥時間の経過と共に感光材料の表
面温度が変化しておく様子を示しており、右の縦軸と破
線の交点は乾燥部の温度を示している。The broken line in FIG. 1 shows how the surface temperature of the photosensitive material changes as the drying time elapses, and the intersection of the right vertical axis and the broken line shows the temperature of the drying section.
第1図より、以下のことが分かる。 The following can be seen from FIG.
乾燥時間の経過につれて、感光材料残留水分率が減少
していくが、感光材料の表面温度は、感光材料残留水分
率がある値に達するまでは一定である。As the drying time elapses, the residual moisture content of the photosensitive material decreases, but the surface temperature of the photosensitive material remains constant until the residual moisture content of the photosensitive material reaches a certain value.
乾燥時間がある値を越えると感光材料残留水分率は滑
らかに減少していくが、感光材料の表面温度は乾燥部の
温度まで上昇する。When the drying time exceeds a certain value, the residual moisture content of the photosensitive material decreases smoothly, but the surface temperature of the photosensitive material rises to the temperature of the drying section.
上記、から感光材料の乾燥には2つの乾燥領域が
生じていることがわかる。これを恒率乾燥域及び減率乾
燥域と呼ぶことにする。From the above, it can be seen that two drying regions are generated in drying the photosensitive material. These will be referred to as a constant rate drying area and a decreasing rate drying area.
恒率乾燥域は、感光材料の両面に付着している水分を
蒸発させるための熱量(以下、感光材料表面の水分の
「蒸発潜熱」と呼ぶ)が、感光材料の内の乳剤に含水し
ている水分を感光材料の表面に出すための使用される熱
量(以下、乳剤層中の水分の「拡散熱量」と呼ぶ)より
多い乾燥域である。従って、乾燥時間の経過と共に感光
材料の残留水分量は減少していくが(実線参照)、感光
材料の表面は濡れている状態なので、感光材料の表面温
度は、乾燥に使用する加熱空気の温度(t℃)よりも低
い温度(tw℃)で略一定に保たれる(破線参照)。In the constant-rate drying area, the amount of heat for evaporating the moisture adhering to both surfaces of the photosensitive material (hereinafter referred to as “evaporation latent heat” of moisture on the surface of the photosensitive material) is contained in the emulsion in the photosensitive material. This is a dry region in which the amount of heat used to release the moisture present on the surface of the light-sensitive material (hereinafter, referred to as the "diffusion heat" of the water in the emulsion layer) is larger. Accordingly, the residual moisture content of the photosensitive material decreases as the drying time elapses (see the solid line). However, since the surface of the photosensitive material is in a wet state, the surface temperature of the photosensitive material is the temperature of the heated air used for drying. It is kept substantially constant at a temperature (tw ° C.) lower than (t ° C.) (see broken line).
減率乾燥域は、感光材料内の乳剤に含水している水分
を感光材料の表面に出すための使用される「拡散熱量」
が、感光材料の両面に付着している水分の蒸発潜熱より
も多い乾燥域である。従って、感光材料表面に移行して
きた水分の蒸発潜熱が少なくなり、感光材料の表面温度
を上昇させる熱量が多くなってしまうので、乾燥時間の
経過と共に感光材料の表面温度が乾燥に使用する加熱空
気の温度(t℃)まで上昇する(破線参照)。The decay rate drying area is the "diffusion heat" used to bring out the moisture contained in the emulsion in the photosensitive material to the surface of the photosensitive material.
Is a dry region in which the latent heat of evaporation of moisture adhering to both surfaces of the photosensitive material is larger. Therefore, the latent heat of evaporation of the moisture transferred to the surface of the photosensitive material decreases, and the amount of heat for increasing the surface temperature of the photosensitive material increases. (T ° C.) (see the broken line).
乾燥中、特に減率乾燥域中、乳剤層中の水分が少なく
なるにつれて、使用される「拡散熱量」が少なくなり、
乳剤層中の含水量が略0になった時が感光材料の乾燥の
終了である。During drying, especially in the rate-decreasing dry area, as the moisture in the emulsion layer decreases, the `` diffusion heat '' used decreases,
The drying of the light-sensitive material is completed when the water content in the emulsion layer becomes substantially zero.
ここで、恒率乾燥域と減率乾燥域の境界となる感光材
料残留水分率を限界含水率と呼び、その点を限界含水点
と呼ぶことにする。Here, the residual moisture content of the photosensitive material, which is the boundary between the constant rate drying area and the decreasing rate drying area, is called a critical moisture content, and that point is called a critical moisture content point.
即ち、限界含水点とは、「蒸発潜熱」が一定である限
界点、具体的には感光材料を乾燥中に、感光材料表面に
付着している水分がほとんど無くなった点である。That is, the critical water content point is a critical point at which the "latent heat of vaporization" is constant, specifically, a point at which moisture adhering to the photosensitive material surface during drying of the photosensitive material has almost disappeared.
第1図は、乾燥部内の温度tを45℃、相対湿度を40%
に保ち、感光材料をコニカ(株)製SRフィルムを使用し
た例である。この場合の限界含水率が10〜25%であり、
恒率乾燥域での感光材料の表面温度twは32℃であった。Fig. 1 shows that the temperature t in the drying section is 45 ° C and the relative humidity is 40%.
This is an example in which a Konica Corporation SR film was used as the photosensitive material. The limit moisture content in this case is 10-25%,
The surface temperature tw of the photosensitive material in the constant-rate drying region was 32 ° C.
限界含水率は感光材料の乳剤膜厚、組成、層構成等に
よって感光材料毎に異なる値であり、また、感光材料の
表面温度twも感光材料及び乾燥条件で異なる値となる。The critical water content varies depending on the photosensitive material depending on the emulsion film thickness, composition, layer structure, etc., and the surface temperature tw of the photosensitive material also varies depending on the photosensitive material and the drying conditions.
以上のことから、乾燥方式の違いによる乾燥ムラは、
温風乾燥方式では恒率乾燥域の乾燥に時間がかかり、赤
外線乾燥方式では恒率乾燥域の乾燥の時間を短縮するこ
とができるが、減率乾燥域での乾燥で過乾燥となること
が原因であることを見出した。From the above, drying unevenness due to the difference in drying method is
In the hot air drying method, it takes time to dry the constant rate drying area.In the infrared drying method, the drying time in the constant rate drying area can be shortened. I found that it was the cause.
この発明はこのような課題を解決するもので、乾燥時
間を短縮して処理能力を向上させつつ、処理液で処理さ
れることより白抜け部及び黒化部が生じる感光材料に特
有の画質劣化を防止でき、仕上がり画質の向上を図れる
感光材料処理装置を提供することを目的としている。The present invention solves such a problem, and shortens the drying time to improve the processing ability, and also causes the image quality degradation peculiar to a photosensitive material in which white spots and blackened parts are caused by processing with a processing solution. It is an object of the present invention to provide a photosensitive material processing apparatus capable of preventing the occurrence of an image and improving a finished image quality.
[課題を解決するための手段] 前記課題を解決し、かつ目的を達成するために、この
発明は、以下のように構成した。[Means for Solving the Problems] In order to solve the problems and achieve the object, the present invention is configured as follows.
請求項1に記載の発明は、 『処理液で処理されることにより白抜け部及び黒化部
が生じる感光材料を処理液で処理する処理部と、 感光材料を乾燥する乾燥部と、 を有する感光材料処理装置において、 前記乾燥部は、恒率乾燥域において赤外乾燥を行い、減
率乾燥域においては赤外乾燥を行わずに温風乾燥を行う
ものであることを特徴とする感光材料処理装置。』であ
る。The invention according to claim 1 includes: “a processing unit that processes a photosensitive material in which a blank portion and a blackened portion are generated by being processed by a processing solution, using a processing solution; and a drying unit that dries the photosensitive material. In the photosensitive material processing apparatus, the drying unit performs infrared drying in a constant-rate drying region, and performs hot-air drying without performing infrared drying in a decreasing-rate drying region. Processing equipment. ].
請求項1記載の発明により、乾燥時間を短縮して処理
能力を向上させつつ処理液で処理されることにより白抜
け部及び黒化部が生じる感光材料に特有の画質劣化の防
止でき、仕上がり画質の向上を図れる。According to the first aspect of the present invention, it is possible to prevent image quality degradation peculiar to a photosensitive material in which white spots and blackened portions are generated by processing with a processing solution while shortening the drying time and improving the processing capacity, and the finished image quality Can be improved.
請求項2に記載の発明は、 『前記処理部が、感光材料を、現像液の次に定着液で
処理するものであることを特徴とする請求項1に記載の
感光材料処理装置。』である。2. The apparatus according to claim 1, wherein the processing section processes the photosensitive material with a fixing solution next to a developing solution. ].
[発明の実施の形態] 以下、この発明の一実施例を添付図面に基づいて詳細
に説明する。Hereinafter, an embodiment of the present invention will be described in detail with reference to the accompanying drawings.
第2図は感光材料処理装置の概略図、第3図は感光材
料処理装置の現像槽の斜視図である。FIG. 2 is a schematic view of a photosensitive material processing apparatus, and FIG. 3 is a perspective view of a developing tank of the photosensitive material processing apparatus.
第2図において、符号Aは露光された感光材料を搬入
する感光材料搬入部、Bは搬入された感光材料を処理す
る処理部、Cは処理された感光材料をスクイズするスク
イズ部、Dは処理された感光材料を乾燥する乾燥部、E
は処理済の感光材料を搬出する感光材料搬出部である。In FIG. 2, reference numeral A denotes a photosensitive material loading unit for loading the exposed photosensitive material, B denotes a processing unit for processing the loaded photosensitive material, C denotes a squeezing unit for squeezing the processed photosensitive material, and D denotes a processing unit. Drying section for drying the photosensitive material
Numeral denotes a photosensitive material unloading section for unloading the processed photosensitive material.
感光材料搬入部A 撮影済の感光材料Fは、装置本体1の上方位置に設け
られた挿入口20から1枚ずつ挿入され、この挿入口20に
は挿入検知センサ21が設けられ、感光材料の挿入を検知
して制御部に入力される。これにより、装置本体1の搬
送系を駆動すると共に、乾燥部Dを駆動して、乾燥温度
を上昇させるようになっている。また、感光材料Fの挿
入を検知して、処理時間に応じた挿入間隔を設定する。Photosensitive Material Loading Port A The photographed photosensitive material F is inserted one by one from an insertion port 20 provided at a position above the apparatus main body 1, and an insertion detection sensor 21 is provided in the insertion port 20 so that the photosensitive material F The insertion is detected and input to the control unit. Accordingly, the transport system of the apparatus main body 1 is driven, and the drying unit D is driven to increase the drying temperature. Further, the insertion of the photosensitive material F is detected, and an insertion interval according to the processing time is set.
この感光材料搬入部Aには、図示しない感光材料幅検
出手段が設けられ、感光材料の場を検出して、その情報
を制御部に出力するようになっており、制御部ではこの
情報から感光材料の面積演算を行ない、処理液補充の基
準としている。The photosensitive material carry-in section A is provided with a photosensitive material width detecting means (not shown) for detecting the location of the photosensitive material and outputting the information to a control section. The area of the material is calculated and used as a reference for replenishing the processing solution.
処理部B 処理部Bには現像槽30、定着槽31、水洗槽32等の処理
槽が備えられ、それぞれに送りローラ群を有する搬送ラ
ック33,34,35,36が着脱可能に設けられており、処理槽
や搬送ラックの洗浄のとき取り外すことができるように
なっている。この搬送ラック33〜36はそれぞれ感光材料
の搬送方向を変えるターン部33a〜36aを有しており、処
理槽の底部で下方から上方へ搬送方向を変える。Processing Unit B The processing unit B is provided with processing tanks such as a developing tank 30, a fixing tank 31, and a washing tank 32, and transport racks 33, 34, 35, and 36 each having a feed roller group are detachably provided. It can be removed when cleaning the processing tank and transport rack. The transfer racks 33 to 36 have turn portions 33a to 36a for changing the transfer direction of the photosensitive material, respectively, and change the transfer direction from below to above at the bottom of the processing tank.
現像槽30と定着槽31との間、定着槽31と水洗槽32との
間には渡り部37,38が備えられ、現像槽30の搬送タック3
3,34で搬送される感光材料は現像液中から渡り部37に送
られ、この渡り部37のローラ群によって現像液をスクイ
ズして定着槽31へ送る。定着槽31では感光材料が搬送ラ
ック35で搬送されて、定着液中から渡り部38へ送り、こ
の渡り部38で定着液をスクイズして水洗槽32へ送り、そ
れぞれ後段の処理槽へ処理液が持込まれることを防止し
ている。Crossover portions 37 and 38 are provided between the developing tank 30 and the fixing tank 31 and between the fixing tank 31 and the washing tank 32.
The photosensitive material conveyed in 3 and 34 is sent from the developing solution to the transfer section 37, and the developing solution is squeezed by the rollers of the transfer section 37 and sent to the fixing tank 31. In the fixing tank 31, the photosensitive material is conveyed by the conveyance rack 35 and sent from the fixing solution to the transfer section 38. The fixing liquid is squeezed in the transfer section 38 and sent to the washing tank 32, and the processing solution is transferred to the subsequent processing tank. Is prevented from being brought in.
現像槽30に備えられた搬送機構はターン部33a,34aを
有する搬送ラック33,34で構成されており、この搬送ラ
ック33,34は感光材料の搬送方向に並列に配置されてお
り、搬送ラック33,34の渡り部39は処理液中に配置さ
れ、この渡り部39で感光材料Fが空気中で出ないで現像
液中で送られ、連続的な現像処理が可能になっている。The transport mechanism provided in the developing tank 30 includes transport racks 33 and 34 having turn portions 33a and 34a.The transport racks 33 and 34 are arranged in parallel in the photosensitive material transport direction. The transfer portions 33 and 34 are disposed in the processing solution, and the photosensitive material F is sent in the developer solution without coming out of the air at the transfer portions 39, thereby enabling continuous development processing.
現像槽30には第3図に示すように、現像液の温度を調
節するための循環系40が備えられており、循環ポンプ41
の駆動で現像槽30の底部に設けた吸い込み部42からパイ
プ43を介してヒータ44へ送り、このヒータ44で加熱した
パイプ45を介して現像槽30の上部に設けた吹き出し部46
から現像液中に循環させ、現像液の温度を一定にしてい
る。現像液の補充は循環系40の循環ポンプ41の前段側又
は後段側に設けた供給部47,48から補充することがで
き、或いは現像槽30の上方に設けた供給部29から補充す
るようにしてもよい。As shown in FIG. 3, the developing tank 30 is provided with a circulating system 40 for adjusting the temperature of the developing solution.
Is driven from a suction part 42 provided at the bottom of the developing tank 30 to a heater 44 via a pipe 43, and a blowing part 46 provided at an upper part of the developing tank 30 via a pipe 45 heated by the heater 44.
And circulates through the developing solution to keep the temperature of the developing solution constant. The developer can be replenished from supply units 47 and 48 provided before or after the circulating pump 41 of the circulation system 40, or supplied from a supply unit 29 provided above the developing tank 30. You may.
現像槽30に配置された搬送ラック33,34は並列に配置
されており、縦方向の長さL1は一個で形成する場合より
約半分程度に短縮され、その分横方向の長さL2で長くな
っている。従って、現像槽30も縦方向の長さが半分に短
縮されて浅くなっており、その分横方向へ長くなってい
る。The transport racks 33 and 34 arranged in the developing tank 30 are arranged side by side, and the length L1 in the vertical direction is reduced to about half as compared with the case where one is formed, and the length L2 in the horizontal direction is correspondingly longer. Has become. Therefore, the length of the developing tank 30 in the vertical direction is reduced by half and becomes shallow, and the length in the horizontal direction is correspondingly increased.
この現像槽30の現像液の温度分布を、第4図の現像槽
に第5図の搬送ラックを設けた場合と比較し、表1及び
表2に示す。The temperature distribution of the developer in the developing tank 30 is shown in Tables 1 and 2 in comparison with the case where the transport rack shown in FIG. 5 is provided in the developing tank shown in FIG.
第4図は比較例の現像槽100を、第5図に比較例の搬
送ラック110を示しており、現像槽100には縦方向に長い
搬送ラック110が配置される。FIG. 4 shows the developing tank 100 of the comparative example, and FIG. 5 shows the transport rack 110 of the comparative example. In the developing tank 100, a vertically long transport rack 110 is arranged.
搬送ラック110は横方向の長さL3は短く、縦方向の長
さL4が長くなっており、搬送長さは第2図及び第3図に
示す実施例の搬送ラック33,34の搬送長さと同様になっ
ている。The transport rack 110 has a shorter horizontal length L3 and a longer vertical length L4, and the transport length is the same as the transport lengths of the transport racks 33 and 34 of the embodiment shown in FIGS. It is similar.
従って、現像槽100はこの搬送ラック110に応じて横方
向は短く、縦方向に長くなっており、循環系40は現槽液
の補充は前記実施例と同様である。Therefore, the developing tank 100 is shorter in the horizontal direction and longer in the vertical direction in accordance with the transport rack 110, and the replenishment of the circulating system 40 with the liquid in the current tank is the same as in the above embodiment.
表1は現像液の設定温度を35.0℃に設定した場合の温
度分布を示しており、温度の測定点は第3図ではa〜j
で行ない、第4図ではA〜Eで行なった。Table 1 shows the temperature distribution when the set temperature of the developer is set to 35.0 ° C., and the temperature measurement points are shown by a to j in FIG.
And in FIGS. 4A to 4E.
第4図の比較例の現像槽100では、縦方向へ長いため
温度分布が0.5℃以上と大きいが、第2図及び第3図に
示す実施例の現像槽30では容積が大きいにもかかわら
ず、縦方向に短いため温度分布を0.2℃以下と小さくな
っている。 In the developing tank 100 of the comparative example shown in FIG. 4, the temperature distribution is as large as 0.5 ° C. or more because it is long in the longitudinal direction, but the developing tank 30 of the embodiment shown in FIGS. In addition, the temperature distribution is as small as 0.2 ° C. or less because it is short in the vertical direction.
表2は第2図及び第3図に示す実施例の現像槽30と、
第4図及び第5図に示す比較例の現像槽100において、
その上部の供給部49、または循環系40から低温(5℃)
の現像液が補充された場合の温度分布を示しており、温
度測定点は前記表1に示す場合と同様である。Table 2 shows the developing tank 30 of the embodiment shown in FIG. 2 and FIG.
In the developing tank 100 of the comparative example shown in FIGS. 4 and 5,
Low temperature (5 ° C) from the supply section 49 above or the circulation system 40
Shows the temperature distribution when the developer is replenished, and the temperature measurement points are the same as those shown in Table 1 above.
この場合も、比較例の現像槽100の温度分布より、こ
の実施例の現像槽30の温度分布が小さくなる。 Also in this case, the temperature distribution of the developing tank 30 of this embodiment is smaller than the temperature distribution of the developing tank 100 of the comparative example.
また、第2図及び第3図で感光材料搬入部Aから搬入
される感光材料Fは、搬送ラック33により現像液の上面
から液中の下方へ搬送され、ターン部33aで方向を変え
て上方へ向けられ、現像液中に設けられた渡り部39で搬
送ラック34へ搬送される。この搬送ラック34でも同様に
して、現像液の上面から液中の下方へ搬送され、ターン
部34aで方向を変えて上方へ向けられ、液外に渡り部37
で定着槽31へ搬送される。2 and 3, the photosensitive material F carried in from the photosensitive material carry-in portion A is transported downward from the upper surface of the developer by the transport rack 33, and is turned upward by the turn portion 33a. And transported to the transport rack 34 by a transfer section 39 provided in the developer. Similarly, in the transport rack 34, the developer is transported downward from the upper surface of the developer, is turned upward by the turn part 34a, and is turned upward.
To the fixing tank 31.
このようにして、感光材料Fは浅い現像槽30の現像液
中をターン部33a,34aと渡り部39の3箇所で方向を変え
て搬送されると温度のバラツキのある現像槽30内を、繰
り返し感光材料Fを搬送されるので、均一な現像処理効
果が得られる。また、この方向変換のとき感光材料Fで
現像液が撹拌され、特別な撹拌手段を用いることなく、
現像液の温度や濃度を一定にすることができる。In this manner, when the photosensitive material F is transported in the developing solution in the shallow developing tank 30 in three different directions, namely, the turn parts 33a and 34a and the crossover part 39, the photosensitive material F passes through the developing tank 30 having a temperature variation. Since the photosensitive material F is transported repeatedly, a uniform developing effect can be obtained. Further, at the time of this direction change, the developer is stirred by the photosensitive material F, and without using a special stirring means,
The temperature and concentration of the developer can be kept constant.
これに対して、第4図及び第5図の比較例では、搬送
ラック110が長くなっており、ターン部が現像槽の底部
の一箇所なので、均一な現像効果を期待できない。ま
た、撹拌作用を期待することができない。On the other hand, in the comparative example shown in FIGS. 4 and 5, the transport rack 110 is long and the turn portion is located at the bottom of the developing tank, so that a uniform developing effect cannot be expected. Further, a stirring action cannot be expected.
この実施例による処理性と比較例の処理性を表3に示
す。Table 3 shows the processability of this example and the processability of the comparative example.
但し、温度分布幅0.5℃は、処理槽に低い温度の処理
液を入れたのち、高い温度の処理液を入れることによっ
て作成した。循環を止めることによっても温度分布幅を
ひろげることができる。However, the temperature distribution width of 0.5 ° C. was prepared by putting a low-temperature processing solution into a processing tank and then adding a high-temperature processing solution. By stopping the circulation, the width of the temperature distribution can be widened.
このように、第4図及び第5図に示す比較例では、現
像液の温度分布があると、1回のUターン搬送だけなの
で、処理画像の銀粒子が一定でなかったり、分布ムラ等
が生じて粒状性に悪くなる。しかも、撹拌作用も小さい
ので、さらにこれらが循環ムラや搬送ローラによって段
ムラ等を生じさせることになり、写真製品の画質が低下
する。 As described above, in the comparative example shown in FIGS. 4 and 5, if there is a temperature distribution of the developing solution, only one U-turn conveyance is performed, so that the silver particles of the processed image are not constant or the distribution unevenness or the like occurs. This results in poor graininess. In addition, since the stirring action is small, these also cause unevenness in circulation or unevenness due to the conveying roller, and the image quality of the photographic product is reduced.
これに対して、この実施例ではターン部が複数あるの
で温度のバラツキのある処理槽であっても、均一な処理
性が得られる。さらに、この実施例では表1,2に示すよ
うに現像液の温度分布が小さく、しかも撹拌作用も感光
材料で行なわれるため、写真製品の画質が向上する。On the other hand, in this embodiment, since there are a plurality of turn portions, uniform processing properties can be obtained even in a processing tank having a temperature variation. Further, in this embodiment, as shown in Tables 1 and 2, the temperature distribution of the developing solution is small, and the stirring action is also performed by the photosensitive material, so that the image quality of the photographic product is improved.
さらに、この実施例では現像槽30が浅くなっており、
処理槽30や搬送ラック33,34を洗浄するとき、搬送ラッ
ク33,34が短く、しかも軽量であるから、処理槽30から
の取出しや組込み、さらに洗浄等での取扱いが容易であ
る。Further, in this embodiment, the developing tank 30 is shallow,
When cleaning the processing tank 30 and the transport racks 33 and 34, the transport racks 33 and 34 are short and lightweight, so that they can be easily taken out and assembled from the processing tank 30, and further handled during cleaning and the like.
なお、この実施例では現像槽30を浅くして、搬送ラッ
ク33,34を2個用いているが、これに限定されず複数で
あれば良い。さらに、定着槽及びその搬送ラックを複数
にして同様に適用することができる。In this embodiment, the developing tank 30 is made shallow and two transport racks 33 and 34 are used. However, the present invention is not limited to this, and a plurality of transport racks may be used. Further, a plurality of fixing tanks and their transport racks can be used in the same manner.
上記の実施例において渡り部を処理液中に設けること
により、処理性が安定する。液外に渡り部があると、液
が空気にもち出されて酸化したり、液外のローラにより
感光材料がスクイズされ、スクイズムラができる等の問
題がある。In the above embodiment, by providing the transition portion in the processing liquid, the processability is stabilized. If there is a crossover portion outside the liquid, there are problems such as the liquid being discharged into the air and being oxidized, and the photosensitive material being squeezed by the roller outside the liquid, causing uneven squeezing.
前記したように、一つの処理槽中に配置された搬送ラ
ックに、感光材料の搬送方向を変えるターン部を複数備
えており、このターン部で感光材料を方向変換して搬送
することで、処理液が撹拌される。さらに、搬送ラック
に複数のターン部を備えることで、縦方向の長さを短縮
することができ、これに応じて処理槽を浅くすることが
可能となり、処理液の温度分布を小さくすることができ
る。As described above, the transport rack arranged in one processing tank is provided with a plurality of turns for changing the transport direction of the photosensitive material, and the turn section changes the direction of the photosensitive material and transports the photosensitive material. The liquid is stirred. Furthermore, by providing the transport rack with a plurality of turns, the length in the vertical direction can be reduced, and accordingly, the processing tank can be made shallower, and the temperature distribution of the processing liquid can be reduced. it can.
さらに、温度分布のある処理槽であっても、複数回繰
り返し搬送されるので、均一な処理性能が得られる。Furthermore, even in a processing tank having a temperature distribution, uniform transfer performance can be obtained because the processing tank is repeatedly transported a plurality of times.
従って、処理液の撹拌手段や処理液の温度調節を行な
う循環系等の特別の手段を用いることなく、簡単な構造
で感光材料の処理ムラを防止でき、感光材料の画質を向
上させることができる。また、ターン部を有する搬送ラ
ックを複数備え、この搬送ラックの渡り部を処理液中に
配置しているから、縦方向に短い複数の搬送ラックで構
成され、これに応じて処理槽が浅くなり、処理槽や搬送
ラックを洗浄するとき、搬送ラックが短く、しかも軽量
であるから、処理中の感光材料が空気にさらされること
がなく、安定した処理を可能にしながら処理槽からの取
出しや取扱いが容易になる。Therefore, it is possible to prevent uneven processing of the photosensitive material with a simple structure and improve the image quality of the photosensitive material without using a special means such as a processing liquid stirring means or a circulation system for controlling the temperature of the processing liquid. . In addition, a plurality of transport racks having a turn portion are provided, and since the transfer portion of the transport rack is disposed in the processing liquid, the transport rack is configured with a plurality of transport racks that are short in the vertical direction, and the processing tank becomes shallower accordingly. When cleaning processing tanks and transport racks, the transport rack is short and lightweight, so that the photosensitive material being processed is not exposed to air, allowing removal and handling from the processing tank while enabling stable processing. Becomes easier.
スクイズ部C スクイズ部Cスクイズ部Cはそのローラ群40によっ
て、感光材料Fの洗浄水を絞り落したり、吸い取って乾
燥部Dに送り、感光材料が効率的に乾燥できるようにし
ている。Squeeze section C Squeeze section C The squeeze section C uses a group of rollers 40 to squeeze or suck the washing water of the photosensitive material F and send it to the drying section D so that the photosensitive material can be dried efficiently.
乾燥部D 乾燥部Dでは感光材料Fが送りローラ50群によって送
られ形成された搬送路Rを搬送される。この乾燥部Dの
前段部には、赤外線ヒータ51、反射板52及びガイド53か
らなり、赤外線ヒータ51の赤外線を入射して乾燥する赤
外線乾燥部D1が配置され、後段部にはスリットノズル54
から水分不飽和加熱空気が感光材料Fへ吹き付けて乾燥
する温風乾燥部D2が配置されている。Drying Section D In the drying section D, the photosensitive material F is transported by the transport rollers 50 and transported along the transport path R formed. An infrared heater 51, a reflection plate 52, and a guide 53 are provided at the front stage of the drying unit D, and an infrared drying unit D1 that receives and dries infrared rays of the infrared heater 51 is disposed.
A hot air drying section D2 is provided for drying the photosensitive material F by blowing moisture-unsaturated heated air onto the photosensitive material F.
この乾燥部Dでは第6図の感光材料の乾燥曲線Aに示
すように、感光材料の恒率乾燥域においては赤外線乾燥
部D1による赤外線乾燥が行なわれ、減率乾燥域において
は温風乾燥部D2による温風乾燥が行なわれる。In the drying section D, as shown by the drying curve A of the photosensitive material in FIG. 6, the infrared drying is performed by the infrared drying section D1 in the constant rate drying area of the photosensitive material, and the hot air drying section is performed in the decreasing rate drying area. Hot air drying with D2 is performed.
一般に感光材料においては黒化部が白抜け部により保
有水分量が多いので、限界含水率を超えて(減率乾燥
域)、限界含水率に至るまで(恒率乾燥域)の乾燥能力
で乾燥を行なうと、白抜け部の乾燥が終了しているにも
かかわらず、黒化部の乾燥が終了していないことにな
る。In general, in a photosensitive material, the blackened portion has a higher moisture content due to the white spots, so that the drying capacity exceeds the limit moisture content (decreasing dry area) and reaches the limit moisture content (constant rate drying area). Is performed, the drying of the blackened portion is not completed even though the drying of the blank portion has been completed.
また、感光材料の層構成、組成によっては、乾燥が進
むにつれて感光材料の表面が硬化してしまう場合があ
り、黒化部分の乳剤内の水分が感光材料表面に移行する
ことができなくなり、乾燥ムラになる場合もある。Further, depending on the layer structure and composition of the photosensitive material, the surface of the photosensitive material may be hardened as the drying proceeds, and moisture in the blackened portion of the emulsion cannot transfer to the surface of the photosensitive material. It may be uneven.
この実施例では、乾燥する感光材料の限界含水率を越
えてからの減率乾燥域で温風乾燥方式を採用することに
より、黒化部と白抜け部とをほぼ同じ速度で乾燥するよ
うにした。その結果、減率乾燥域において、感光材料の
硬化等の変質を生じないで、且つ感光材料を均一に乾燥
することが可能にある。In this embodiment, by adopting a hot air drying method in a reduced-rate drying area after exceeding the critical moisture content of the photosensitive material to be dried, the blackened portion and the white spot are dried at substantially the same speed. did. As a result, it is possible to dry the photosensitive material uniformly without causing deterioration such as hardening of the photosensitive material in the decreasing rate drying region.
また、恒率乾燥域においては、限界含水率までは乾燥
能力の高い赤外線乾燥方式を採用したので、黒化部にか
かわらず迅速な乾燥が可能になる。In addition, in the constant-rate drying region, since an infrared drying method having a high drying ability is employed up to the limit moisture content, quick drying is possible regardless of the blackened portion.
この実施例について、第6図を用いて詳細に説明す
る。第6図の乾燥曲線Bは温風乾燥方式のみで乾燥工程
を行なった場合の感光材料残留水分率と乾燥時間のグラ
フ、乾燥曲線Cは赤外線乾燥方式のみで乾燥工程を行な
った場合の感光材料残留水分率と乾燥時間のグラフ、乾
燥曲線Aがこの実施例の乾燥方式を用いた場合の感光材
料残留水分率と乾燥時間のグラフである。This embodiment will be described in detail with reference to FIG. The drying curve B in FIG. 6 is a graph of the residual moisture content of the photosensitive material and the drying time when the drying step is performed only by the hot air drying method, and the drying curve C is the photosensitive material when the drying step is performed only by the infrared drying method. A graph of the residual moisture content and the drying time, and a drying curve A is a graph of the photosensitive material residual moisture content and the drying time when the drying method of this embodiment is used.
第6図より、赤外線乾燥方式のみで乾燥を行なった場
合、乾燥時間が最も短いことがわかるが、前述のように
限界含水率を超えてからも(減率乾燥域)赤外線乾燥方
式で乾燥を行なうと、乾燥ムラが生じてしまい易い。従
って、この実施例では赤外線乾燥方式で、感光材料の限
界含水率近くまで乾燥を行ない、それ以降を温風乾燥方
式を行なうことで乾燥ムラを防止している。From FIG. 6, it can be seen that the drying time is the shortest when the drying is performed only by the infrared drying method, but the drying is performed by the infrared drying method even after exceeding the limit moisture content (reduction rate drying area) as described above. If performed, drying unevenness is likely to occur. Therefore, in this embodiment, the drying is performed to near the critical moisture content of the photosensitive material by the infrared drying method, and thereafter the drying is performed by the hot air drying method to prevent uneven drying.
恒率乾燥と減率乾燥の判別を判別手段200で行ない、
処理部で処理された感光材料の物理特性に基づいて感光
材料の恒率乾燥域と減率乾燥域とを判別する。この判別
に基づいて制御手段201で感光材料の恒率乾燥域におい
ては赤外乾燥手段202である赤外線ヒータ51を用いて赤
外乾燥を行ない、減率乾燥域においては温風乾燥手段20
3を用いて温風乾燥を行なう。この判別手段200は感光材
料の表面温度を測定し、ある温度以上で識別したり、ま
た感光材料の含水量を測定し、ある含水率で識別した
り、また乾燥部内の温度上昇の傾きにより識別すること
が可能であり、このように構成することで、判別手段20
0の構成が簡単になる。The discrimination between constant rate drying and reduced rate drying is performed by the discriminating means 200,
A constant rate drying area and a reduced rate drying area of the photosensitive material are determined based on the physical characteristics of the photosensitive material processed by the processing unit. Based on this determination, the control means 201 performs infrared drying using the infrared heater 51 as the infrared drying means 202 in the constant rate drying area of the photosensitive material, and performs the hot air drying means 20 in the decreasing rate drying area.
Dry with warm air using 3. This discriminating means 200 measures the surface temperature of the photosensitive material and discriminates it at a certain temperature or higher, or measures the moisture content of the photosensitive material and discriminates it by a certain water content, or discriminates by the slope of the temperature rise in the drying unit. It is possible to make the determination means 20
The configuration of 0 is simplified.
第1の実施例では、赤外線ヒータ51の乾燥能力を、乾
燥部内を感光材料が通過する時間内に、感光材料の含水
率が100%から予め測定しておいた感光材料の限界含水
率まで乾燥するように設定しておくことにより、恒率乾
燥域を赤外線乾燥によって行なうようにした。この場
合、使用する感光材料の限界含水率を、感光材料の表面
温度の測定、含水量の測定等により予め求めておく必要
がある。使用する感光材料の種類による限界含水率にバ
ラツキが無い場合は、赤外線ヒータ51の能力を一定に保
てば良いが、使用する感光材料の種類による限界含水率
にバラツキがある場合は、使用する感光材料によって赤
外線ヒータ51の能力を設定しなおす必要があり、手動で
切り換えたり、感光材料の種類を検出することにより赤
外線ヒータ51の能力を切り換えるようにする。このよう
に構成することで、感光材料や処理状態に応じた乾燥が
可能になる。In the first embodiment, the drying capability of the infrared heater 51 is changed from 100% of the moisture content of the photosensitive material to the previously determined limit moisture content of the photosensitive material within the time when the photosensitive material passes through the drying section. By setting so as to perform the drying, the constant-rate drying area was performed by infrared drying. In this case, the critical moisture content of the photosensitive material to be used must be determined in advance by measuring the surface temperature of the photosensitive material, measuring the water content, and the like. If there is no variation in the critical moisture content depending on the type of photosensitive material used, the capacity of the infrared heater 51 may be kept constant, but if there is variation in the critical moisture content depending on the type of photosensitive material used, use the heater. It is necessary to reset the capability of the infrared heater 51 according to the photosensitive material, and the capability of the infrared heater 51 is switched manually or by detecting the type of the photosensitive material. With this configuration, drying according to the photosensitive material and the processing state can be performed.
また、第7図に示すように、乾燥部D1内に判別手段30
0と、赤外線ヒータ51のON,OFF制御を行なう制御手段301
を設けることにより、判別手段300の情報に基づいて赤
外線乾燥手段である赤外線ヒータ51のON,OFF制御を行な
うようにしても良い。この場合の判別手段300は、乾燥
部内の温度上昇の傾きを測定する温度センサーであり、
温度センサーの情報から、赤外線ヒータ51の能力を制御
することで、恒率乾燥域を赤外線乾燥によって行なうよ
うにした。判別手段300は、感光材料の表面温度、感光
材料の含水の測定する測定手段に置き換えても可能であ
る。Further, as shown in FIG. 7, the discriminating means 30 is provided in the drying section D1.
0 and control means 301 for performing ON / OFF control of the infrared heater 51
The ON / OFF control of the infrared heater 51, which is the infrared drying means, may be performed based on the information of the determination means 300. The determination means 300 in this case is a temperature sensor that measures the slope of the temperature rise in the drying unit,
By controlling the capability of the infrared heater 51 from the information of the temperature sensor, the constant-rate drying region is performed by infrared drying. The determining means 300 can be replaced with a measuring means for measuring the surface temperature of the photosensitive material and the moisture content of the photosensitive material.
この実施例による乾燥画質評価を、遠赤外線乾燥方
式、近赤外線乾燥方式、温度乾燥方式と比較して表4に
示す。Table 4 shows the evaluation of dry image quality according to this example in comparison with the far-infrared drying method, near-infrared drying method, and temperature drying method.
このように、この実施例の赤外線+温風乾燥方式は、
遠赤外線乾燥方式及び近赤外線乾燥方式と比較して画質
が向上し、温風乾燥方式と比較して乾燥能力が向上す
る。 Thus, the infrared ray + hot air drying method of this embodiment is as follows.
The image quality is improved as compared with the far-infrared drying method and the near-infrared drying method, and the drying ability is improved as compared with the warm-air drying method.
乾燥部Dで蒸発した水分は排気ダクト60を介して、処
理部Bの排気ダクト61からの排気と共に、排気ファン62
の駆動によって外部へ排出される。The moisture evaporated in the drying section D is exhausted through the exhaust duct 60 and exhausted from the exhaust duct 61 of the processing section B together with the exhaust fan 62.
Is discharged to the outside by the drive of.
感光材料搬出部E 装置本体1の感光材料搬入部Aと反対側には、感光材
料搬出部Eが設けられ、そのバスケット70内に現像処理
された後、乾燥された処理済の感光材料Fが排出され
る。Photosensitive material unloading section E A photosensitive material unloading section E is provided on the side of the apparatus main body 1 opposite to the photosensitive material unloading section A. After developing processing is performed in the basket 70, dried and processed photosensitive material F is provided. Is discharged.
[発明の効果] 処理液で処理されることにより白抜け部及び黒化部が
生じる感光材料に特有の画質劣化を防止できる。[Effect of the Invention] It is possible to prevent image quality degradation peculiar to a photosensitive material in which white spots and blackened portions are generated by processing with a processing solution.
第1図は乾燥時間と感光材料残留水分率の関係及び乾燥
時間と感光材料の表面温度の関係を示す図、第2図はこ
の発明の感光材料処理装置の概略図、第3図はこの発明
の感光材料処理装置内の現像槽の斜視図、第4図は比較
例の感光材料処理内の現像槽の斜視図、第5図は比較例
の現像槽内のラック構成を示す図、第6図はこの発明の
感光材料処理装置の乾燥部での感光材料の乾燥曲線を示
す図、第7図はこの発明の第2の実施例の感光材料処理
装置の概略図である。 図中符号Dは乾燥部、D1は赤外線乾燥部、D2は温風乾燥
部、200,300は判別手段、201,301は制御手段、202は赤
外線乾燥手段、203は温風乾燥手段である。FIG. 1 is a diagram showing the relationship between the drying time and the residual moisture content of the photosensitive material, and the relationship between the drying time and the surface temperature of the photosensitive material. FIG. 2 is a schematic diagram of the photosensitive material processing apparatus of the present invention. FIG. 4 is a perspective view of a developing tank in the photosensitive material processing of the comparative example, FIG. 4 is a perspective view of a developing tank in the photosensitive material processing apparatus of the comparative example, FIG. FIG. 7 is a diagram showing a drying curve of the photosensitive material in a drying section of the photosensitive material processing apparatus of the present invention, and FIG. 7 is a schematic diagram of a photosensitive material processing apparatus of a second embodiment of the present invention. In the figure, reference symbol D denotes a drying unit, D1 denotes an infrared drying unit, D2 denotes a hot air drying unit, 200 and 300 denote discriminating units, 201 and 301 denote control units, 202 denotes an infrared drying unit, and 203 denotes a hot air drying unit.
フロントページの続き (72)発明者 藤阪 登志男 東京都日野市さくら町1番地 コニカ株 式会社内 (56)参考文献 特開 平3−102348(JP,A) 特開 平2−149845(JP,A) 特開 平2−140741(JP,A) (58)調査した分野(Int.Cl.7,DB名) G03D 15/02 Continuation of the front page (72) Inventor Toshio Fujisaka 1 Sakuracho, Hino-shi, Tokyo Inside Konica Corporation (56) References JP-A-3-102348 (JP, A) JP-A-2-149845 (JP, A) JP-A-2-140741 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) G03D 15/02
Claims (2)
び黒化部が生じる感光材料を処理液で処理する処理部
と、 感光材料を乾燥する乾燥部と、 を有する感光材料処理装置において、 前記乾燥部は、恒率乾燥域において赤外乾燥を行い、減
率乾燥域においては赤外乾燥を行わずに温風乾燥を行う
ものであることを特徴とする感光材料処理装置。An apparatus for processing a photosensitive material, comprising: a processing section for processing a photosensitive material that generates white spots and blackened areas by processing with the processing liquid, using a processing liquid; and a drying section for drying the photosensitive material. The photosensitive material processing apparatus, wherein the drying section performs infrared drying in a constant rate drying area and performs hot air drying without performing infrared drying in a decreasing rate drying area.
定着液で処理するものであることを特徴とする請求項1
に記載の感光材料処理装置。2. The processing section according to claim 1, wherein the processing section processes the photosensitive material with a developing solution followed by a fixing solution.
3. A photosensitive material processing apparatus according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2060606A JP3002683B2 (en) | 1989-04-06 | 1990-03-12 | Photosensitive material processing equipment |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8775289 | 1989-04-06 | ||
JP1-87752 | 1989-04-06 | ||
JP2060606A JP3002683B2 (en) | 1989-04-06 | 1990-03-12 | Photosensitive material processing equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0354560A JPH0354560A (en) | 1991-03-08 |
JP3002683B2 true JP3002683B2 (en) | 2000-01-24 |
Family
ID=26401682
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2060606A Expired - Fee Related JP3002683B2 (en) | 1989-04-06 | 1990-03-12 | Photosensitive material processing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3002683B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04319955A (en) * | 1991-04-19 | 1992-11-10 | Fuji Photo Film Co Ltd | Drying device for automatic developing machine |
JP2977731B2 (en) * | 1994-11-25 | 1999-11-15 | 西本産業株式会社 | Film drying apparatus and method of using the same |
JP4631402B2 (en) * | 2004-11-12 | 2011-02-16 | ノーリツ鋼機株式会社 | Photo processing device |
-
1990
- 1990-03-12 JP JP2060606A patent/JP3002683B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0354560A (en) | 1991-03-08 |
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