JPS6360982B2 - - Google Patents

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Publication number
JPS6360982B2
JPS6360982B2 JP61025284A JP2528486A JPS6360982B2 JP S6360982 B2 JPS6360982 B2 JP S6360982B2 JP 61025284 A JP61025284 A JP 61025284A JP 2528486 A JP2528486 A JP 2528486A JP S6360982 B2 JPS6360982 B2 JP S6360982B2
Authority
JP
Japan
Prior art keywords
raw seaweed
seaweed
treatment
discrete
water content
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP61025284A
Other languages
Japanese (ja)
Other versions
JPS62181762A (en
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 filed Critical
Priority to JP61025284A priority Critical patent/JPS62181762A/en
Priority to KR1019860003944A priority patent/KR900000963B1/en
Priority to CN86103698A priority patent/CN1007777B/en
Publication of JPS62181762A publication Critical patent/JPS62181762A/en
Publication of JPS6360982B2 publication Critical patent/JPS6360982B2/ja
Granted legal-status Critical Current

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L17/00Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
    • A23L17/60Edible seaweed

Description

【発明の詳細な説明】[Detailed description of the invention]

a 産業上の利用分野 本発明は生海苔の処理方法に関する。 b 従来の技術 生海苔の処理法として従来、板状製品化のため
に細断、抄製、乾燥処理が行なわれ、真空凍結乾
燥品化のために真空凍結、ほぐし、乾燥処理が行
なわれ、保存のために脱水、ほぐし、凍結保管処
理が行なわれている。これらの処理中、ほぐし処
理は、人手によるか回転羽根中に海苔の塊りを通
過させる方法がとられている。 c 発明が解決しようとする課題 従来のほぐし処理は、いずれも表面付着水の除
去が十分にされないまま行われるので、ほぐし処
理後も葉体どうしの付着は当然さけられない。従
つてバラ乾燥品を得ようとする場合は、乾燥後に
さらにほぐし操作が必要であり、これはかなり困
難な作業であつた。もし乾燥前に葉体どうしの付
着を防ぐ処理方法があれば、バラ乾燥品も容易に
得られる。また生海苔を冷凍保管する場合も、従
来のほぐし処理のように単に非塊状にするだけで
なく、海苔の葉体どうしの面付着をなくした状態
にしておけばより速やかな凍結及び解凍が期待で
きる。 d 課題を解決するための手段 本発明は、主として厚さ30μm以上の葉片から
なる生海苔を真水または塩類溶液にて洗浄、脱水
し、この海苔を少なくとも葉体が相互付着を起こ
さない含水率迄乾燥雰囲気中にて、付着の生じて
いる海苔葉体に撹拌羽根やガス噴射等によつて、
瞬間的打撃を与えることにより海苔葉体同士を引
き離す離散処理を行うことを特徴とするものであ
る。この処理を行なうことによりその後の乾燥処
理又は凍結処理を行つた場合に葉体どうしの面付
着のない海苔を得ることができる。 本発明において、厚さ30μm以上の葉体はこれ
を90%以上含む生海苔を用いることが好ましく、
厚さ30μm以上の葉片が90%未満の場合、葉体ど
うしの面付着を無くすることが困難になる。 第1図は本発明を実施するための装置の1例で
あり、実験1〜3に使用したものである。図中1
は直径400mm、長さ500mm網目16メツシユのドラム
状乾燥篭、2は回転軸でこれに撹拌羽根(回転直
径390mm)3が互生位置に16枚配されている。4
は乾燥空気の吹出口である。 実験1 この実験では各種離散条件が海苔の離散終了時
含水率とその離散状態とにおよぼす影響を調べ
た。 まず厚さ30μm以上の葉片を95%含み、葉長2
〜5cmの愛知県産生海苔を真水で洗浄し、遠心脱
水して乾燥篭1に投入した。回転軸2を回し撹拌
羽根3にて海苔に瞬間的打撃を与えることによつ
て海苔を離散させるとともに、乾燥空気を乾燥篭
1の下方から上方に向けてほぼ均等な分布で吹出
口4より通風した。 一定時間後撹拌を止め、そのまま通気乾燥を続
け、乾燥後、海苔の離散状態を観察した。結果は
表−1にみられる如く、乾燥空気の温湿度、風
量、海苔投入量により設定される乾燥速度や撹拌
羽根先端速度の違いにかかわらず、概ね含水率
400%の時点迄離散処理を行えば、海苔の良好な
る離散状態が得られることが判つた。但し撹拌羽
根先端速度が1m/秒未満の時は含水率400%を
割つていたにもかかわらず離散が不十分であつ
た。なお、離散状態の判定は、葉体同士の付着が
10%未満を良好、10%以上を不良とした。 実験2 この実験では、海苔の離散頻度が離散状態に及
ぼす影響を調べた。離散は生海苔0.6Kg、風量40
m3/分、温度50℃、湿度15%RH、撹拌羽根先端
速度1.0及び2.0m/秒の条件下で行い、離散頻度
は撹拌羽根を配した回転軸の回転数調節及び間欠
稼動により調整した。離散処理を5分間行つたと
ころで通風乾燥に移し、表−2のような結果を得
た。海苔の離散頻度が40回/分以上でないと撹拌
中、ダマが形成され、良好な離散状態は得られな
かつた。 実験3 この実験では、洗浄液として塩類溶液を使用し
た場合、その種類と濃度が離散処理に及ぼす影響
を調べた。生海苔を0〜4%濃度の各種塩類溶液
にて洗浄し1000回転/分、5分間遠心脱水した。
第2図はこの時の洗浄脱水含水率を示したもので
あり、表−3は、第2図に表示された値の詳細を
示す。同表にみられるように洗浄液の塩の種類に
より傾きは異るが、高濃度になるほど低下してい
る。 さらにこれを投入量0.6Kg、1.2Kg、風量40m3
分、温度50℃、湿度15%RH、撹拌羽根先端速度
2m/秒、離散頻度170回/分の条件にて離散処
理した。洗浄液が食塩水の場合を第3図に示した
が、高濃度になるほど低含水率域迄離散処理を行
わねば良好な離散状態は得られない。 このときの離散処理に要した時間は洗浄液の食
塩濃度が高いほど短い傾向にあり、離散処理時の
初期含水率即ち洗浄脱水含水率に影響されるよう
である。 食塩濃度が4%程度になると、海苔の撹拌羽根
への付着、絡みが多く歩止まりが悪くなるため3
%以下が好ましい。 良好なる離散状態を得るための離散処理終了時
含水率の上限は第3図より食塩濃度をX%とした
とき(400−33X)%であらわされる。他の塩類
溶液でも食塩水の場合と傾きが異るだけであり、
その塩分濃度に換算係数を乗じ、食塩相当濃度X
%としてやれば、食塩水の場合と同様に離散処理
終了時含水率上限は(400−33X)%で示される。
表−4に換算係数の例を示した。 以下に実施例を示す。いずれの実施例も実験3
と同様な離散処理を行つたが、洗浄液として実施
例1では真水を、実施例2では2%塩化マグネシ
ウム溶液を使用した。このときの良好なる離散状
態を得るための離散処理終了時含水率上限はそれ
ぞれ400% 400−33×2×0.88=342%となる。 実施例 1 生海苔1.2Kgを真水で洗浄し、遠心脱水後、離
散処理を7分間行い、含水率を372%とした。こ
れを真空凍結乾燥したところ、良好なる海苔のバ
ラ乾燥品200gを得ることができた。 実施例 2 生海苔0.6Kgを2%塩化マグネシウム溶液で洗
浄、脱水して3分間離散処理を行つたところ、下
表のとおり良好なる離散状態が得られた。
a. Industrial Application Field The present invention relates to a method for processing raw seaweed. b. Conventional technology Traditionally, raw seaweed has been processed by shredding, papermaking, and drying to produce plate-shaped products, and vacuum freezing, loosening, and drying to produce vacuum freeze-dried products. For preservation, they are dehydrated, loosened, and frozen. During these treatments, the loosening process is carried out either manually or by passing the nori clumps through a rotating blade. c Problems to be Solved by the Invention In all conventional loosening treatments, the water adhering to the surface is not sufficiently removed, so it is natural that the adhesion of leaf bodies to each other cannot be avoided even after the loosening treatment. Therefore, in order to obtain a dried product in bulk, it is necessary to further loosen the product after drying, which is a rather difficult task. If there is a treatment method that prevents the adhesion of leaves to each other before drying, it would be easy to obtain dried pieces. In addition, when storing raw seaweed in a frozen state, it is expected that it will freeze and thaw more quickly if it is not only made into non-clumps as in the conventional loosening process, but also the sheets of seaweed are kept from sticking to each other. can. d Means for Solving the Problems The present invention involves washing and dehydrating fresh seaweed, mainly consisting of leaf pieces with a thickness of 30 μm or more, with fresh water or a salt solution, and reducing the seaweed to a moisture content that does not cause mutual adhesion of the leaf bodies. In a dry atmosphere, the adhered seaweed leaves are treated with stirring blades, gas injection, etc.
This method is characterized by performing a discrete process of separating the seaweed leaves from each other by applying an instantaneous blow. By carrying out this treatment, it is possible to obtain seaweed in which the leaves do not stick to each other when a subsequent drying treatment or freezing treatment is performed. In the present invention, it is preferable to use raw seaweed containing 90% or more of this for the leaves with a thickness of 30 μm or more,
If less than 90% of the leaflets have a thickness of 30 μm or more, it becomes difficult to eliminate surface adhesion of the leaflets to each other. FIG. 1 shows an example of an apparatus for carrying out the present invention, which was used in Experiments 1 to 3. 1 in the diagram
2 is a drum-shaped drying basket with a diameter of 400 mm and a length of 500 mm and 16 meshes, and 2 is a rotating shaft on which 16 stirring blades (rotating diameter of 390 mm) 3 are arranged in alternating positions. 4
is a dry air outlet. Experiment 1 In this experiment, the effects of various discrete conditions on the moisture content of seaweed at the end of the discrete period and its discrete state were investigated. First, it contains 95% leaf pieces with a thickness of 30 μm or more, and has a leaf length of 2.
~5 cm of seaweed produced in Aichi Prefecture was washed with fresh water, dehydrated by centrifugation, and placed in drying basket 1. By turning the rotating shaft 2 and giving an instantaneous blow to the seaweed with the stirring blade 3, the seaweed is dispersed, and the dry air is ventilated from the air outlet 4 in an almost even distribution from the bottom to the top of the drying basket 1. did. After a certain period of time, stirring was stopped, air drying was continued, and after drying, the discrete state of the seaweed was observed. As shown in Table 1, the results show that, regardless of the temperature and humidity of the drying air, the air volume, the drying speed set by the amount of seaweed input, and the speed of the tip of the stirring blade, the moisture content generally remains the same.
It was found that if the discrete processing was performed up to the 400% point, a good discrete state of the seaweed could be obtained. However, when the stirring blade tip speed was less than 1 m/sec, the dispersion was insufficient even though the water content was below 400%. Note that the determination of discrete state is based on the fact that the leaves are not attached to each other.
Less than 10% was considered good, and 10% or more was bad. Experiment 2 In this experiment, we investigated the effect of the discrete frequency of seaweed on the discrete state. Discrete raw seaweed 0.6Kg, air volume 40
m 3 /min, temperature 50°C, humidity 15% RH, stirring blade tip speed 1.0 and 2.0 m/s, and the discrete frequency was adjusted by adjusting the rotation speed and intermittent operation of the rotating shaft on which the stirring blade was arranged. . After performing the discrete treatment for 5 minutes, the sample was transferred to ventilation drying, and the results shown in Table 2 were obtained. Unless the frequency of dispersing the seaweed was 40 times/min or more, clumps were formed during stirring, and a good dispersion state could not be obtained. Experiment 3 In this experiment, when a saline solution was used as a cleaning solution, the influence of its type and concentration on discrete processing was investigated. Raw seaweed was washed with various salt solutions of 0 to 4% concentration and dehydrated by centrifugation at 1000 revolutions/minute for 5 minutes.
FIG. 2 shows the water content of washing and dehydration at this time, and Table 3 shows details of the values displayed in FIG. 2. As shown in the table, the slope differs depending on the type of salt in the cleaning solution, but it decreases as the concentration increases. Furthermore, the amount of input is 0.6Kg, 1.2Kg, and the air volume is 40m 3 /
Discrete treatment was carried out under the following conditions: temperature: 50° C., humidity: 15% RH, stirring blade tip speed: 2 m/sec, dispersion frequency: 170 times/min. FIG. 3 shows the case where the cleaning solution is saline, but as the concentration increases, a good discrete state cannot be obtained unless the discrete treatment is performed in the low water content range. The time required for the discrete treatment at this time tends to be shorter as the salt concentration of the cleaning liquid is higher, and it seems to be influenced by the initial water content during the discrete treatment, that is, the water content of cleaning and dehydration. When the salt concentration is around 4%, the seaweed tends to stick to the stirring blades and become tangled, resulting in poor yields.
% or less is preferable. From FIG. 3, the upper limit of the water content at the end of the discrete process to obtain a good discrete state is expressed as (400-33X)% when the salt concentration is X%. For other salt solutions, the only difference is that the slope is different from that of saline solution.
The salt concentration is multiplied by the conversion factor, and the salt equivalent concentration
If expressed as %, the upper limit of water content at the end of discrete treatment is expressed as (400-33X)%, as in the case of saline water.
Table 4 shows examples of conversion factors. Examples are shown below. Experiment 3 for both examples
A discrete treatment similar to that described above was carried out, but fresh water was used as the cleaning liquid in Example 1, and a 2% magnesium chloride solution was used in Example 2. At this time, the upper limit of the moisture content at the end of the discrete processing to obtain a good discrete state is 400% (400-33 x 2 x 0.88 = 342%). Example 1 1.2 kg of raw seaweed was washed with fresh water, centrifugally dehydrated, and then subjected to discrete treatment for 7 minutes to reach a water content of 372%. When this was freeze-dried in a vacuum, 200 g of good dried seaweed pieces could be obtained. Example 2 When 0.6 kg of raw seaweed was washed with a 2% magnesium chloride solution, dehydrated, and dispersed for 3 minutes, a good dispersed state was obtained as shown in the table below.

【表】 e 発明の効果 本発明の処理はそのほぐし効果により海苔の表
面積を増大させるため、その後の処理例えば真空
凍結乾燥や熱風乾燥時の乾燥処理、凍結処理、解
凍処理等の効率化が期待でき、これら処理時間の
短縮や省エネルギー化を図ることができる。また
乾燥前処理として行えばバラ乾燥品という新しい
海苔の形を生み出し、消費の多様化にも対応する
ことができる。
[Table] e Effects of the invention Since the treatment of the present invention increases the surface area of seaweed due to its loosening effect, it is expected to improve the efficiency of subsequent treatments such as vacuum freeze drying, drying treatment during hot air drying, freezing treatment, thawing treatment, etc. It is possible to shorten these processing times and save energy. Furthermore, if it is performed as a pre-drying treatment, a new form of dried seaweed can be created, which can be used to meet the diversification of consumption.

【表】【table】

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明を実施するための装置の一例を
示す概念図である。第2図は洗浄液塩分濃度と海
苔の脱水時含水率との関係を示した図、第3図は
食塩洗浄液が離散処理終了時含水率と離散状態と
の関係におよぼす影響を示した図である。 1……ドラム状乾燥篭、2……回転軸、3……
撹拌羽根、4……乾燥空気の吹出口。
FIG. 1 is a conceptual diagram showing an example of an apparatus for implementing the present invention. Figure 2 is a diagram showing the relationship between the salt concentration of the cleaning solution and the moisture content during dehydration of seaweed, and Figure 3 is a diagram showing the influence of the saline cleaning solution on the relationship between the moisture content at the end of the discrete process and the discrete state. . 1... Drum-shaped drying basket, 2... Rotating shaft, 3...
Stirring blade, 4...Dry air outlet.

Claims (1)

【特許請求の範囲】 1 主として厚さ30μm以上の葉片からなる生海
苔を洗浄液にて洗浄脱水し、少なくとも海苔葉体
が相互付着を起こさない含水率迄乾燥雰囲気中に
て、付着の生じている海苔葉体に瞬間的打撃を与
えることにより海苔葉体同士を引き離す離散処理
を行うことを特徴とする生海苔の処理方法。 2 上記生海苔が厚さ30μm以上の葉片を90%以
上含むことを特徴とする特許請求の範囲第1項記
載の生海苔の処理方法。 3 上記洗浄液が真水であり、離散処理を含水率
が約400%になるまで行うことを特徴とする特許
請求の範囲第1項記載の生海苔の処理方法。 4 上記洗浄、脱水後の含水率が450〜800%であ
ることを特徴とする特許請求の範囲第3項記載の
生海苔の処理方法。 5 上記洗浄液が3%以下の塩水であることを特
徴とする特許請求の範囲第1項記載の生海苔の処
理方法。 6 上記塩水の濃度がX%のとき、離散処理を含
水率が(400−33X)%になるまで行うことを特
徴とする特許請求の範囲第5項記載の生海苔の処
理方法。 7 上記離散処理を撹拌羽根付きの回転横軸をも
つ通気性容器内で、容器内に通風させながら乾燥
雰囲気中にて行うことを特徴とする特許請求の範
囲第1項記載の生海苔の処理方法。 8 上記離散処理の離散頻度が40回/分以上、撹
拌羽根先端速度が1m/秒以上であることを特徴
とする特許請求の範囲第7項記載の生海苔の処理
方法。 9 上記離散処理をして得た生海苔をバラ乾燥処
理又は凍結処理に付することを特徴とする特許請
求の範囲第1項記載の生海苔の処理方法。
[Scope of Claims] 1. Raw seaweed mainly consisting of leaf pieces with a thickness of 30 μm or more is washed and dehydrated with a cleaning solution, and the seaweed leaves are dried in a dry atmosphere to a moisture content that does not cause mutual adhesion. A method for processing raw seaweed, characterized by performing a discrete process of separating the seaweed fronds from each other by applying an instantaneous blow to the seaweed fronds. 2. The method for processing raw seaweed according to claim 1, wherein the raw seaweed contains 90% or more of leaf pieces with a thickness of 30 μm or more. 3. The method for treating raw seaweed according to claim 1, wherein the cleaning liquid is fresh water, and the discrete treatment is performed until the water content reaches about 400%. 4. The method for treating raw seaweed according to claim 3, wherein the water content after washing and dehydration is 450 to 800%. 5. The method for treating raw seaweed according to claim 1, wherein the cleaning liquid is salt water containing 3% or less. 6. The method for treating raw seaweed according to claim 5, characterized in that when the concentration of the salt water is X%, the discrete treatment is performed until the water content reaches (400-33X)%. 7. The treatment of raw seaweed as set forth in claim 1, characterized in that the above-mentioned discrete treatment is carried out in an air-permeable container having a rotating horizontal axis equipped with stirring blades in a dry atmosphere while ventilation is provided inside the container. Method. 8. The method for treating raw seaweed according to claim 7, wherein the frequency of the discrete treatment is 40 times/min or more, and the stirring blade tip speed is 1 m/sec or more. 9. The method for processing raw seaweed according to claim 1, characterized in that the raw seaweed obtained by the above-mentioned discrete treatment is subjected to bulk drying treatment or freezing treatment.
JP61025284A 1986-02-07 1986-02-07 Treatment of raw laver Granted JPS62181762A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP61025284A JPS62181762A (en) 1986-02-07 1986-02-07 Treatment of raw laver
KR1019860003944A KR900000963B1 (en) 1986-02-07 1986-05-21 Apparatus for treating of laver
CN86103698A CN1007777B (en) 1986-02-07 1986-06-06 The processing method of fresh laver

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61025284A JPS62181762A (en) 1986-02-07 1986-02-07 Treatment of raw laver

Publications (2)

Publication Number Publication Date
JPS62181762A JPS62181762A (en) 1987-08-10
JPS6360982B2 true JPS6360982B2 (en) 1988-11-28

Family

ID=12161719

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61025284A Granted JPS62181762A (en) 1986-02-07 1986-02-07 Treatment of raw laver

Country Status (3)

Country Link
JP (1) JPS62181762A (en)
KR (1) KR900000963B1 (en)
CN (1) CN1007777B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1037895C (en) * 1995-06-19 1998-04-01 曹振福 Making method for dried plate shape undaria pinnatifida
KR101285227B1 (en) * 2010-06-25 2013-07-11 서진기장영어조합법인 A method for stroring fresh undaria pinnatifida
CN102366128B (en) * 2010-09-21 2012-12-26 王行安 Airflow backflushing material-loosing device for seaweed processing
CN103859013A (en) * 2014-02-18 2014-06-18 海安县兰波实业有限公司 Method for preserving porphyra yezoensis
CN103859003A (en) * 2014-04-02 2014-06-18 蔡祥山 Method for keeping purple laver fresh

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5726567A (en) * 1980-07-21 1982-02-12 Koasa Shoji Kk Freeze preservation of raw laver leaf
JPS59187766A (en) * 1983-04-11 1984-10-24 Shirako:Kk Preparation of nonlamellar laver product

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5726567A (en) * 1980-07-21 1982-02-12 Koasa Shoji Kk Freeze preservation of raw laver leaf
JPS59187766A (en) * 1983-04-11 1984-10-24 Shirako:Kk Preparation of nonlamellar laver product

Also Published As

Publication number Publication date
KR870007666A (en) 1987-09-21
CN1007777B (en) 1990-05-02
JPS62181762A (en) 1987-08-10
CN86103698A (en) 1987-08-19
KR900000963B1 (en) 1990-02-23

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