Jiaxiang Zhang

Background and Objectives: Dry grinding pea starch (DG) and wet grinding pea starch (WG) are two primary industrial starches with significantly different structures, physicochemical properties, and application potentials. To date, there have been no detailed studies examining these differences. Therefore, the aim of this study was to (i) investigate the effects of dry grinding and wet grinding on the structure of pea starch, and (ii) examine how the structure of pea starch influences its physicochemical properties and digestibility.Findings: The crystallinity (35.75%), medium and long amylopectin (AP) chains (22.00%), swelling power (17.23 g/g), gelatinization temperature (76.4°C), and gelatinization viscosity (5585.0 cP) of WG were higher than those of DG (24.29%, 20.36%, 16.90 g/g, 75.9°C, and 5196.3 cP). In contrast, the average particle size (APS) (24.31 μm), resistant starch content (45.80%), and gel hardness (509.70 g) were lower than those of DG (25.68 μm, 52.13%, and 617.53 g).Conclusions: Significant structural differences exist between WG and DG, with APS and AP chain length distribution being the primary factors contributing to the distinct physicochemical characteristics of the two pea starches.Significance and Novelty: This is the first detailed comparison of the properties of commercial pea starch produced by two different processes. The results provide theoretical insights that underpin the use of pea starch in functional foods and promote the development of new starch‐based products.

In this study, proteins were prepared from Schizochytrium pombe residue after oil extraction using isoelectric point precipitation, and their physicochemical and emulsifying properties were investigated. Our objective was to assess the suitability of these proteins for functional ingredient applications. Through a one-way experiment and optimization using response surface design, the effects of time, temperature, pH, and the material–liquid ratio of NaOH alkaline extraction were explored. The isoelectric point is verified by isoelectric point precipitation; the results revealed that crude protein from Schizochytrium (SCP) is minimally soluble at pH 4.2. Compared with whey protein (WP), it promotes better emulsion stability through the emulsification test. This study suggests that Schizochytrium oil-processing byproducts represent a promising source of protein, with potential applications as functional ingredients, offering implications for the usage of these byproducts in various industries.

Pectin is widely used in the food and pharmaceutical industries. However, data on sweet potato pectin extraction and structural property analyses are lacking. Here, for the high-value utilization of agricultural processing waste, sweet potato residue, a byproduct of sweet potato starch processing, was used as raw material. Ammonium oxalate, trisodium citrate, disodium hydrogen phosphate, hydrochloric acid and citric acid were used as extractants for the pectin constituents, among which ammonium oxalate had a high extraction rate of sweet potato pectin, low ash content and high molecular weight. Structural and gelation analyses were conducted on ammonium oxalate-extracted purified sweet potato pectin (AMOP). Analyses showed that AMOP is a rhamnogalacturonan-I-type pectin, with a molecular weight of 192.5 kg/mol. Chemical titration and infrared spectroscopy analysis confirmed that AMOP is a low-ester pectin, and scanning electron and atomic force microscopy demonstrated its linear molecular structure. Gelation studies have revealed that Ca²⁺ is the key factor for gel formation, and that sucrose significantly enhanced gel hardness. The highest AMOP gel hardness was observed at pH 4, with a Ca²⁺ concentration of 30 mg/g, pectin concentration of 2%, and sucrose concentration of 40%, reaching 128.87 g. These results provide a foundation for sweet potato pectin production and applications.

In order to improve the utilization value of the erythritol mother liquor, the separation and purification of the erythritol mother liquor was selected in this study. The selected chromatographic separation programme for erythritol crystallizing mother liquor is as follows: Firstly, erythritol is resolved from mannitol and arabitol with DTF-01Ca (Suqing Group) resin and then mannitol is resolved from arabitol with 99Ca/320 (Dowex) resin. At the same time, the chromatographic conditions of the DTF-01Ca (Suqing Group) and 99Ca/320 (Dowex) resins were optimized, resulting in an optimal separation temperature and mobile phase flow rate of 70 degrees C, 10 ml/min. On this basis, a single-column chromatographic model was used to calculate the TD model parameter (N) and the mass transfer coefficient (km ) of the separation of erythritol mother liquor by DTF-01Ca (Suqing Group) and 99Ca/320 (Dowex) resins. The adsorption isotherms, TD model parameter (N) and the mass transfer coefficient (km ) provides data references for the design and operation of the simulated moving beds (SMB) separation system for the industrial-scale separation of erythritol crystallizing mother liquor.

Starch production from fresh sweet potatoes generates process wastewater called sweet potato cell liquid (SPCL), which is rich in sweet potato protein (SPP). Currently, the commonly used protein recovery methods, such as isoelectric point precipitation and ultrafiltration, were not suitable for...

Acetoin (AC) is an important platform compound with two enantiomers (R)-AC and (S)-AC. Due to its unique spatial structure, optically pure AC has particularly high application in asymmetric synthesis. Highly optically pure AC could be produced from glucose using biofermentation technology. In this paper, we have observed that the recovered AC product from the fermentation broth containing (R)-AC was a racemic mixture. The changes of the enantiomeric excess (e.e.) of (R)-AC enantiomers in the feed solution during the recovery process were then investigated, confirming that the racemization occurs during solvent distillation. Further studies showed that high temperature is the main factor affecting the conversion of the two enantiomers, while low temperature significantly prevents this conversion reaction. Therefore, we optimized the solvent recovery process and used vacuum distillation to reduce the distillation process temperature, which effectively prevented the racemization: obtains AC products with more than 98% purity and successfully maintained the proportion of (R)-AC above 96%. To our knowledge, this is the first report on the factors affecting the enantiomeric purity in the downstream extraction process of AC production by fermentation.