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Calstar 

操作及保養

明書

 

OPERATION AND MAINTENANCE 

HANDBOOK

 

A10Ex

 

 

                                            16 

during the storage; in particular formation of peroxides with some oxygenated compounds and some 

ketones.

)

 

 

回收過程中

溶劑之品質降級劣化

. (

Degradation of solvents during the solvent recovery 

treatment.

)

 

 

溫度影響下

﹐造成硝酸鹽類物質劣化

(

如:硝酸甲

).

 (Degradation of nitrate compounds 

under temperature effect (ex. nitromethane).) 

 

由於缺乏安定劑

產生腐蝕性物質

(

如:鹽酸

). (

Formation of corrosive compounds determined 

by the lack of stabilizer (ex.  hydrochloric acid).

)

 

 

特性殘渣之分解

(

如:硝化纖維素

). (

Decomposition of certain residues (ex. nitrocellulose).

)

 

 

混合不相容之物質在一起

(

如添加

氧化劑

﹕硝酸加入可燃性混合物裏

). (

Mixtures of 

incompatible products (presence of a strong oxidizer, such as nitric acid, in a mixture of flammable 

products).

)

 

5.3 

化學風險

:

刺激性

﹑毒性

 (

Chemical risks: irritation, poisoning

 

    

接觸溶劑液體或暴露在溶劑蒸汽中

﹐可能會刺激皮膚及眼睛﹔另外﹐吸入過量溶劑蒸

汽至肺中

﹐可能會造成眩暈甚至中毒

     (

The contact with the liquids or the exposition to the steams can damage your skin or eyes. 

Whereas the inhalation of solvent steams will cause toxic risks.)

 

 

6.0 

綜合注意事項

 (

GENERAL WARNINGS

 

 

在回收操作過程中

如果設定加熱

溫度過高

﹐某些類殘渣在蒸餾將要結束後

,

可能會過熱而

冒煙

(

如含硝化纖維素之硝基油漆殘渣

);

此時

,

請不要驚慌

,

關掉電源

,

讓機器自行冷卻即可

亦可外力吹風或灑水

幫助降溫

.

嚴禁打開回收桶上蓋

!!

由於殘渣過熱

,

打開桶蓋將有大量

氧氣

進入回收桶極易發生起火

!!

 (During the working procedure, if the distillation temperature is set 

too high, some types of residues will overheat and emit smoke (for example: nitrogen cellulose from 

nitro-painting residues). When this happens, please remain calm, cut out the electrical feeding of the 

unit, and let the unit cool down. External forces fanning or sprinkling water can help lower the 

temperature. However, do NOT open the tank lid!! Due to overheated residues. Opening the lid will 

allow large amounts of oxygen into the tank, running a high-risk of fire!!) 

 

溫度控制器設定錯誤會造成殘渣過熱而冒煙

 , 

﹕丙酮沸點

56

 

﹐若關機溫度控制器之設

定高出或太接近

56

﹐機器將無法自動關機﹐持續加熱﹐引起殘渣過熱冒煙﹔熱媒油加熱溫

度設定太高也會造成殘渣過熱冒煙

 (

Incorrect setting of the thermostats may result into 

overheating residues and emission of smoke. For example: the boiling point of acetone is 56°C. If 

the automatic-cut-off thermostat temperature is set too close to 56°C or any higher, the unit cannot 

automatically turn off. The unit will continue heating, causing the residues to overheat and emit 

smoke. If the Heat Transfer Oil heating temperature is set too high, it will also cause the residues to 

overheat and emit smoke.

)

 

 

 

不要將不同操作過程

產生之廢溶劑倒入桶內一起回收

. (

In the unit tank, do not combine 

products from different working cycles.

)

 

 

不要將回收桶作溶劑儲存桶

.

要開始蒸餾回收溶劑之前

﹐才將溶劑加入回收桶

. (

Do not use 

the tank as solvents storage. Fill the tank just before starting the distillation cycle.

)

 

 

在回收操作過程中

﹐無論任何情形切勿打開桶蓋

!!! 

 Do NOT, for any reason, open the lid during the working phases!!

 

Summary of Contents for Calstar A10Ex

Page 1: ...CONTACT 866 774 4531 EMAIL SALES OLYMPIC EQUIPMENT COM 18935 59TH AVE NE ARLINGTON WA 98223 SOLVENT RECOVERY MACHINE OPERATION AND MAINTENANCE HANDBOOK Calstar A10Ex...

Page 2: ...AINTENANCE HANDBOOK A10Ex 2 A10Ex Parts Description 01 Frame 02 shell 03 Ex Tag 04 machine tag 05 shotpin of tank cover 06 tank cover 07 beam of tank cover 08 safety valve 09 locking structure 10 tank...

Page 3: ...OPERATION AND MAINTENANCE HANDBOOK A10Ex 3 12 venting valve 13 electrical box 14 sealed screw of exhaust heat transfer oil 15 Ex heater 16 handle 17 outlet of recovered solvent 18 steam temp meter 19...

Page 4: ...Unpacking Page 14 9 0 Installation Page 14 9 1 Unit set up on the floor Page 15 10 0 Setting at work Page 15 10 1 Electrical connection Page 15 10 2 Pipe connection for recovered solvent Page 16 11 0...

Page 5: ...Calstar OPERATION AND MAINTENANCE HANDBOOK A10Ex 5 23 0 Scrapping Page 29 24 0 Appendix The Properties of Various Solvents Page 30 0 0 SYMBOLOGY...

Page 6: ...0Ex 6 No Water apply to the fire No Smoking Any Fire is prohibited Don t Touch High Temperature Area Using Glasses during the job Using Gas mask during the job Using Gloves during the job Don t Touch...

Page 7: ...umption The self protections of this equipment are Overload Protection System Emergency Shutoff Protection System Over Timing Protection System Over Pressure Protection System Over Heat Protection Sys...

Page 8: ...em for Solvent Recovery Machine with label ExdIIBT6 The design of Anti Explosion matches the government requirement of GB3836 1 2010 and GB3836 2 2000 The electric cable matches the government require...

Page 9: ...mum surface temperature group T5 100 Explosive mixture level ANTI EXPLOSION model ANTI EXPLOSION labeling of products 1 4 2 2 Basic parameters Applied Voltage AC110V Applied Frequency 50 60Hz Applied...

Page 10: ...sive mixture level ANTI EXPLOSION model ANTI EXPLOSION labeling of products 1 4 4 2 Basic parameters Applied Voltage AC110V Applied Frequency 50 60Hz Applied Currency DKX60Ex 32A 1 5 Working environme...

Page 11: ...for replacements The unauthorized replacement is prohibited After overhauling and when assembling secure the screws and bolts to their according places and fixed tight Any use of the Solvent Recovery...

Page 12: ...f while exceeding the normal recovery time the timer will automatically stop the distillation cycle the electro blowing fan will continue to operate cooling down the temperature until the unit automat...

Page 13: ...DESCRIPTION OF MAIN COMPONENTS MATERIAL The ANTI EXPLOSION surface frame of the control box heater and the air compressors are made of aluminum alloy SS304 The tank and the tank lid are made of SS304...

Page 14: ...ration and Maintenance Handbook during operation the Solvent Recovery Machine may cause residues to overheat and emit smoke The main reasons are as followed If the residues within the Solvent Recovery...

Page 15: ...hine After 12 hours of cooling thoroughly clean the tank If the unit is not fully cool down opening the tank lid will ignite a fire 2 Working environment should have correct ventilation and efficient...

Page 16: ...or example nitrogen cellulose from nitro painting residues When this happens please remain calm cut out the electrical feeding of the unit and let the unit cool down External forces fanning or sprinkl...

Page 17: ...vent steams In order to avoid dangerous emissions of steams it is necessary not to open the lid when the steam thermometer temperature is lower than the boiling point of the treated product 6 1 2 Pay...

Page 18: ...load tiled or cemented if possible The electrical outlet place must matches the local regulation regarding to the Settlement of the solvent recovery manipulator treatment The Solvent Recovery machine...

Page 19: ...the work place It is necessary for the presence of a feeding sectioning device by manual control This device is able to allow the separation of the unit electrical equipment from the general feeding...

Page 20: ...carefully and learn the terminology and the controls function of the unit in a correct and exhaustive way 11 0 CONTROLS 11 0 1 A10Ex IC A10Ex Control Box and IC Control Panel displayed below Control...

Page 21: ...to be recovered It is therefore necessary to know the technical characteristics of the specific solvent to be recovered and in particular its boiling point The thermostats setting must be executed by...

Page 22: ...e timer settings should be set as followed Upon the first use of the unit assistance is required throughout its working T1 T2 3hrs Set the timer with the 3 hours as described in the picture When switc...

Page 23: ...s overheating and emission of smoke After complete control box setting remember to screw up the control box tightly Under any circumstances don t change or replace the control box parts by yourself An...

Page 24: ...18 Maximum absorption 9 5 A Power Voltage 110 60HZ ACV HZ Control Voltage 24 DCV Heating method HTM indirect heating oil Length 655 Width 505 Height 1050 Weight 62 Kg Working temperature 50 190 Ideal...

Page 25: ...on of electrostatic charges bunching 13 2 Check of the steam pipes and lid seal This check must be executed before every distillation cycle and is necessary to make sure of the absence of obstructions...

Page 26: ...rking efficiency if the solvent is foamy or very thick appropriately reduce the input capacity Clean the edges of the lid and close the lid 13 1 Place an empty and clean tank for the recovered solvent...

Page 27: ...n cycle Never open for any reason the lid before the end of the distillation cycle 16 0 RESIDUALS DISCHARGE AND UNIT CLEANING Pictured below The tank must be cleaned from residuals at the end of every...

Page 28: ...Clean the inside of the tank from all the distillation residuals using if necessary a non metallic and not a sharpened tool Clean the tank upper edge and the lid seal from distillation residuals to gu...

Page 29: ...led workers 18 0 CLEANING At least once a month keep the condenser carter and wings free from dust and or fouling to avoid the efficiency decrease of the steam cooling system For cleaning it is suffic...

Page 30: ...Institute of Chemical Co Neo SK OIL TOTAL K3120 ESSOTHERM 550 DIATHERM 80 etc It is necessary to make sure that the oil does not have a humidity rate more than 2 In fact the presence of water in the...

Page 31: ...device and spare parts are prohibited Promptly replace the seal for the electricity importing device when it wears out or degenerates The manufacturer has spare parts To purchase it please contact the...

Page 32: ...and the automatic switching off at the end of the cycle D The unit does not recover all of the polluted solvent content Check if the setting of the thermostats is correct E The unit works but the rec...

Page 33: ...there is a leakage within the lid please replace it with a new one Check the state of the seal H The solvent comes out hot Check if the electro blowing fan works correctly Check if the electro blowin...

Page 34: ...ene 137 000 0 8540 03 Trimethylbenzene 164 700 0 8650 04 Tetramethylbenzene 205 000 0 9020 05 Ethyl acetate 77 000 0 9000 06 Butyl acetate n 126 300 0 8820 07 Butyl acetate sec 112 200 0 8700 08 Monog...

Page 35: ...000 1 3492 25 Perchloroethylene 121 200 1 6230 26 Trichloroethylene 87 190 1 4640 27 MEK Methyl ethylketone 79 640 0 8049 28 Acetone 56 100 0 7905 29 Methylisobutylketone 115 900 0 8000 30 Cyclohexano...

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