用塔式反应器回收豆腐乳清废水中的蛋白质:初步结果

Intan Permatasari, A. Senania, F. Dara, A. Sholihah, Sambas Sambas, Achmad Syamsudin, M. Muchlis, Widyarani Widyarani
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引用次数: 0

摘要

非营利组织知道,污水会产生浓的废水或乳清(凝乳),后者的pH值低,有机物高,因此如果处理不当,会导致环境污染。另一方面,蛋白质的一种浓知性废物可以被利用来减少环境污染的潜力,并将进一步加工成具有经济价值的产品。本研究的目的是获得初步数据,以评估从浓豆腐废物中恢复蛋白质的可行性。我们研究中浓缩的已知废物的蛋白质浓度为3115毫克/l。实验是在半冲程模式下使用立柱似锦反应堆进行的。三次空气流量(每小时10,30和60 l/小时)和三次已知的集中废物(10、50和100%)测试。实验结果表明,初始蛋白质浓度影响蛋白质的恢复,因此需要大约3000毫克/l的初始蛋白质浓度。1.0±0.5,相当于最高比例浓缩蛋白质6±4%的复兴,实现对流量10 l /小时而在知道浓缩废物100%集中。流量增加至30 l /小时浓缩比例没有改变(0,9±0.2),但恢复蛋白质增加71±为14%。对于其他参数,如初始蛋白质浓度、浑浊的组成、气流速率、气泡大小、水合物密度和反应堆设计,还需要进一步的研究。被称为苔藓的高生水力学分解,它具有低pH和高有机质物质,因此在不污染特性的情况下可能存在环境污染。另一方面,另一种截然不同的蛋白质,这种namely constitution可以从废水中回收其环境潜力,并作为一种产生经济价值的产品进一步进行加工。这项研究可以先验数据以确定使用泡沫分解的方法从豆腐wastewater恢复蛋白质的方法。在我们的研究中,豆腐的作用是3115毫克的L-1。实验使用的是半批次模式中的列根排版反应堆。三次空气流动的混合(10,30和60 L -1)和三次豆腐流的融合(10,50和100%)是测试的。我们的推荐显示,最初的蛋白质集中恢复,蛋白质集中接近3000毫克。L-1所需。《最高enrichment ratio of 1。0±0。5,哪种corresponded恢复到6±4%的蛋白质,是100% achieved at 10 L . h - 1流率和乳清双臀。Increasing 30 L . h - 1的流动速率nid not change the enrichment ratio(0。9±0。2),但要恢复increased《蛋白质71±为14%。进一步的研究需要对这样的初始蛋白质集中、whey合成、水流动速率、气泡大小、气泡时间和反应堆设计进行parameters。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Protein Recovery from Tofu Whey Wastewater Using a Column Reactor: Preliminary Results
ABSTRAK Industri tahu menghasilkan air limbah pekat atau whey (dadih), yang memiliki pH rendah dan bahan organik yang tinggi, sehingga dapat menyebabkan pencemaran lingkungan jika tidak diolah dengan baik. Di sisi lain, salah satu kandungan limbah tahu pekat yaitu protein dapat dimanfaatkan kembali untuk mengurangi potensi pencemaran lingkungan dan diolah lebih lanjut menjadi produk yang bernilai ekonomis. Penelitian ini bertujuan untuk mendapatkan data awal untuk menilai kelayakan penggunaan metode fraksinasi busa untuk pemulihan protein dari limbah tahu pekat. Limbah tahu pekat dalam penelitian kami memiliki konsentrasi protein awal 3.115 mg/l. Percobaan dilakukan dengan menggunakan reaktor fraksinasi busa berbentuk kolom dalam mode semi-curah. Kombinasi tiga laju alir udara (10, 30, dan 60 l/jam) dan tiga konsentrasi limbah tahu pekat (10, 50, dan 100%) diuji. Hasil percobaan menunjukkan bahwa konsentrasi protein awal mempengaruhi pemulihan protein, sehingga diperlukan konsentrasi protein awal sekitar 3.000 mg/l. Rasio pengayaan tertinggi 1,0 ± 0,5, setara dengan pemulihan protein 6 ± 4%, dicapai pada laju alir 10 l/jam dan konsentrasi limbah tahu pekat 100%. Peningkatan laju alir hingga 30 l/jam tidak mengubah rasio pengayaan (0,9 ± 0,2), tetapi meningkatkan pemulihan protein hingga 71 ± 14%. Penelitian lebih lanjut diperlukan untuk parameter-parameter lain seperti konsentrasi protein awal, komposisi limbah tahu pekat, laju aliran udara, ukuran gelembung, holdup cairan, dan desain reaktor. ABSTRACT The tofu industry generates highly-polluted wastewater called whey, which has a low pH and high organic matter, and therefore can cause environmental pollution when not treated properly. On the other hand, one of the whey constituents namely protein can be recovered from the wastewater to reduce its environmental potency and to be further processed as a product that has an economic value. This study aimed to obtain preliminary data to assess the feasibility of using the foam fractionation method for the recovery of protein from tofu whey wastewater. Tofu whey in our study had an initial protein concentration of 3115 mg.L-1. The experiment was performed using a column foam fractionation reactor in a semi-batch mode. Combinations of three air flow rates (10, 30, and 60 L.h-1) and three tofu whey concentrations (10, 50, and 100%) were tested. Our results show that initial protein concentration influenced protein recovery, with a protein concentration of approximately 3000 mg.L-1 required. The highest enrichment ratio of 1.0 ± 0.5, which corresponded to 6 ± 4% protein recovery, was achieved at 10 L.h-1 flow rate and 100% whey concentration. Increasing the flow rate to 30 L.h-1 did not change the enrichment ratio (0.9 ± 0.2), but increased the protein recovery to 71 ± 14%. Further investigation is needed for parameters such as initial protein concentration, whey composition, air flow rate, bubble size, holdup time, and reactor design.  
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