企鵝專家簡介油脂浸出車間需要的技能與參數(shù)
油脂浸出設(shè)備; 企鵝專家簡介油脂浸出車間需要的技能與參數(shù)
The skills and parameters of the oil extraction workshop in the oil extraction workshop
(1)技能參數(shù):
(1) skill parameters:
?、龠M浸出器料胚質(zhì)量 直接浸出技能,料胚厚度為0.3毫米以下,水分10%以下;預(yù)榨浸出技能,餅塊大對角線不逾越15毫米,粉末度(30目以下)5%以下,水分5%以下。
In the leaching process, the quality of the embryo is directly leached, the thickness of the material is 0.3 mm, the moisture content is below 10%, the pre pressing and extraction techniques, the maximum diagonal of the cake block is not exceeding 15 mm, and the powder (30 mesh) is below 5%.
?、诹吓咴谄睫D(zhuǎn)浸出器中浸出,其轉(zhuǎn)速不大于100轉(zhuǎn)/分鐘;在環(huán)型浸出器中浸出,其鏈速不小于0.3轉(zhuǎn)/分鐘。
II blank in flat turn leacher leaching, the speed is not more than 100 rpm; leaching in the circular extractor, the chain speed of not less than 0.3 revolutions per minute.
③浸出溫度50~55℃。
Leaching temperature 50 ~ 55.
④混合油濃度 入浸料胚含油18%以上者,混合油濃度不小于20%;入浸料胚含油大于10%者,混合油濃度不小于15%;入浸料胚含油在大于5%、小于10%者,混合油濃度不小于10%。
4 mixed oil concentration in leaching material embryo oil 18% or more and the concentration of mixed oil not less than 20%; in leaching material embryo oil is more than 10% who, mixed oil concentration is not less than 15%; immersing into blank oil in more than 5%, less than 10% who, mixed oil concentration is not less than 10%.
?、萜稍谡裘搶拥亩毫魰r間,高溫粕不小于30分鐘;蒸脫機氣相溫度為74-80℃;蒸脫機粕出口溫度,高溫粕不小于105℃,低溫粕不大于80℃。帶冷卻層的蒸脫機(DTDC)粕出口溫度不逾越環(huán)境溫度10℃。
The meal in the steaming off layer sojourn time, high temperature meal not less than 30 minutes; desolventizer toaster gas phase temperature 74-80 DEG C; desolventizer toaster meal outlet temperature, hot meal is not less than 105 DEG C, meal low temperature not more than 80 DEG C. The outlet temperature of the cooling layer (DTDC) is not exceed the ambient temperature at 10.
?、藁旌嫌驼舭l(fā)系統(tǒng) 汽提塔出口毛油含總揮發(fā)物0.2%以下,溫度105℃。
The mixed oil stripper export crude oil evaporation system containing total volatiles below 0.2%, temperature 105.
?、呷軇┗厥障到y(tǒng) 冷凝器冷卻水進口水溫30℃以下,出口溫度45℃以下。凝集液溫度40℃以下。
The solvent recovery system of condenser cooling water inlet temperature of 30 DEG C, the outlet temperature of 45 DEG C. The condensation temperature of liquid was below 40.
(2)產(chǎn)品質(zhì)量:
(2) product quality:
①毛油總揮發(fā)物0.2%以下。②粕殘油率1%以下(粉狀料2%以下),水分12%以下,引爆實驗合格。
Total volatile oil of hair oil is below 0.2%. The rate of residual oil in the oil is below 1% (2% below), the moisture content is below 12%, and the detonation experiment is qualified.
?、弁ǔ┣竺偷诌_如下標(biāo)準(zhǔn):色澤、氣味、滋味正常;水分及揮發(fā)物0.5%;雜質(zhì)0.5%;酸價參看材料質(zhì)量標(biāo)準(zhǔn),不高于規(guī)則懇求。
3 usually begged crude oil arrived in the standard as follows: color, smell, taste normal; 0.5% moisture and volatile matter; 0.5% of impurities; acid value is referred to the criteria of the quality of materials, not more than rules begged.
?、茴A(yù)榨餅質(zhì)量,在預(yù)榨機出口處查驗,懇求:餅厚度12毫米;餅水分6%;餅殘油;13%,但根據(jù)浸出技能需求,可提高到18%。
4 pre pressing cake quality, inspection at the outlet of the pre press machine, pleading, the cake thickness of 12 mm; cake moisture 6%; cake oil residue; 13%, but according to the leaching skill requirements, increased to 18%.
(3)有關(guān)設(shè)備核算選用的參數(shù):料胚密度(γ)400~45O千克/米3 ;餅塊密度(γ) 560~620千克/米3;層式蒸炒鍋總傳熱系數(shù)K=628千焦/(米2•時•℃);
(3) account for equipment selection of parameters: material embryo density (gamma) 400 ~ 45o kg / M 3; cake bulk density (gamma) 560 to 620 kg / 3 meters; layer type steaming wok overall heat transfer coefficient K=628 kJ / M 2 - when - C);
入浸出器料胚的容重,大豆粕按360千克/米3,預(yù)榨餅按600千克/米3,浸出時間90分鐘。
The bulk density of the embryo of the leaching unit, the soybean meal was 360 kg / M 3, the pre pressing cake was 600 kg / M 3, the leaching time was 90 minutes.
有關(guān)列管式傳熱設(shè)備的總傳熱系數(shù),常壓蒸發(fā)應(yīng)不低于下列數(shù)據(jù):一蒸發(fā)器總傳熱系數(shù)1170千焦/(米2•時•℃);二蒸發(fā)器總傳熱系數(shù)420千焦/(米2•時•t);溶劑冷凝器的總傳熱系數(shù)754千焦/(米2•時•℃);溶劑加熱器的總傳熱系數(shù)420千焦/(米2•時•℃)
The total heat transfer coefficient of relevant equipment for shell and tube heat transfer, atmospheric evaporation should be not less than the following data: the overall heat transfer coefficient of the first evaporator 1170 kJ / (M 2 - - C); the overall heat transfer coefficient of the second evaporator 420 kJ / (2 m - - t); the total heat transfer coefficient of solvent condenser 754 kJ / (M 2 - when - C); the total heat transfer coefficient of solvent heater 420 kJ / (M 2 - - C)
設(shè)備安置應(yīng)緊湊,在充沛考慮操作修補的空間后,可考慮車間首要通道為1.2米,兩設(shè)備出色有些距離如需操作人員通過則為0.8米,如不考慮操作人員通過可為0.4米。
Equipment placement should be compact, in full consideration of the space after the operation of the operation, can consider the workshop the first channel is 1.2 meters, two of the equipment is excellent, some distance such as the need to operate the staff through the 0.8 meters, if not considered by the operator can be 0.4 meters.
靠墻面無人路過的貯槽與墻距離為0.2米。如有管路通過,上述標(biāo)準(zhǔn)需求考慮管子及保溫層所占空間。車間內(nèi)禁絕設(shè)地坑、管溝避免溶劑蒸氣堆集。
By the wall of the wall and the wall is no passing distance of 0.2 meters. If there is a line through, the above standard needs to consider the space of the pipe and insulation layer. In the workshop, a ban pit trench to avoid solvent vapor accumulation.
(4)消耗方針:蒸汽消耗量500(350)千克/噸料;電消耗量15千瓦•時/噸料;冷卻水量20(30)噸/噸料;溶劑消耗量<5千克/噸料
(4) consumption of 500 (350) kg / ton of steam consumption, 15 kwh of electricity consumption, 20 (30) tons / ton of cooling water, and the solvent consumption of <5 kg / ton
留心:蒸汽消耗量中,括號內(nèi)數(shù)字為負(fù)壓蒸發(fā)技能消耗數(shù)。
Pay attention: the amount of steam consumption, the number of brackets in the negative pressure evaporation skills.
(5)管路系統(tǒng)規(guī)劃 對每條管線進行管徑核算,一同按輸送的材料選擇所需管的類型質(zhì)料。每條管線應(yīng)進行編號,并編制管路、閥門、疏水器、外表明細(xì)表。
(5) pipeline system planning for each pipeline to carry out the pipe diameter calculation, together with the transport of materials to choose the type of material required. Each line should be numbered, and the preparation of pipelines, valves, traps, the appearance of the table.
浸出車間管徑核算,可選用流速數(shù)據(jù)如下:主蒸氣管25米/秒,支蒸氣管20米/秒,水管1.5米/秒,混合油溶劑管1.0米/秒。
The calculation of the pipe diameter of the leaching plant can be used to select the flow rate data as follows: the main steam pipe is 25 m / s, the steam pipe is 20 m / s, the water pipe is 1.5 m / s and the mixed oil solvent is 1 m / sec.
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