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Kamzolova, S.V. Citric Acid Production by Yarrowia lipolytica Yeast. Encyclopedia. Available online: https://encyclopedia.pub/entry/56580 (accessed on 29 April 2024).
Kamzolova SV. Citric Acid Production by Yarrowia lipolytica Yeast. Encyclopedia. Available at: https://encyclopedia.pub/entry/56580. Accessed April 29, 2024.
Kamzolova, Svetlana V.. "Citric Acid Production by Yarrowia lipolytica Yeast" Encyclopedia, https://encyclopedia.pub/entry/56580 (accessed April 29, 2024).
Kamzolova, S.V. (2024, April 11). Citric Acid Production by Yarrowia lipolytica Yeast. In Encyclopedia. https://encyclopedia.pub/entry/56580
Kamzolova, Svetlana V.. "Citric Acid Production by Yarrowia lipolytica Yeast." Encyclopedia. Web. 11 April, 2024.
Citric Acid Production by Yarrowia lipolytica Yeast
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This entry is adapted from the peer-reviewed paper 10.3390/pr11123435

Citric acid (CA) and its derivatives, including salts and esters, are in high demand across various manufacturing sectors. The fungus Aspergillus niger is mainly used for the commercial production of CA, using sucrose and molasses as the primary carbon sources. Since the 1960s, researchers have been working intensively to introduce Yarrowia lipolytica yeast as an alternative to traditional fungal technology.

microbial synthesis citric acid properties and applications Yarrowia lipolytica yeast

1. Introduction

Citric acid (CA) and its derivatives, including salts and esters, are in high demand across various manufacturing sectors. According to the Global Citric Acid Market Outlook (2023) [1], the world market for CA reached a volume of approximately 2.59 million tons in 2022, and is projected to increase to 3.29 million tons by 2028. About 70% of global CA production is dedicated to the food industry, while 12% is allocated to pharmacological preparations, and 18% is used in technical applications [2].
Currently, the fungus Aspergillus niger is the most commonly used producer for commercial CA production, using sucrose and molasses as the main carbon sources. The fungus A. niger offers several advantages. These include ease of cultivation, high concentration, and specific rate of CA production, as well as refined nutrient media and cultivation conditions. The drawbacks of using fungal CA technology involve the reality that molasses typically contain around 44–54% fermentable sugars, 20% non-sugar substances, and 8–12% mineral compounds, including a considerable number of heavy metals. As a result, the maximum product yield (YCA) generally falls within 50–70% of the molasses consumed. It is necessary to treat the molasses with potassium hexacyanoferrate or other complexing compounds to eliminate excessive trace elements. This production of CA poses environmental hazards due to the accumulation of substantial solid and liquid waste, resulting in high disposal costs. Additionally, the A. niger production process emits an air mixture containing spores, which are potent allergens causing respiratory illnesses like aspergillosis [3][4].
Since the 1960s, researchers have been working intensively to introduce Yarrowia lipolytica yeast as an alternative to traditional fungal technology. Y. lipolytica yeast can produce CA from various carbon sources. In addition, Y. lipolytica is more tolerant to low pH, resulting in significant cost reductions. Y. lipolytica yeast exhibits a high tolerance towards high concentrations of carbon sources and impurities present within substrates. Additionally, Y. lipolytica yeast cultivation processes can be easily scaled and automated [3][4][5][6][7]. Y. lipolytica yeast, as well as products based on its synthesis, are generally recognized as safe (GRAS) and can be used in food, medicine, and pharmacology [5].

2. Properties and Applications

Citric acid (CA) exists in two forms: an anhydrous form and a monohydrate form (food grade). Table 1 outlines the main characteristics of the two forms.
Table 1. Physicochemical properties of CA (based on [3][8][9]).
Index Form of CA
Monohydrate Anhydrous
IUPAC Name 2-hydroxypropane-1,2,3-tricarboxylic acid hydrate 2-hydroxypropane-1,2,3-tricarboxylic acid
Molecular formula C6H8O7·H2O C6H8O7
Chemical formula CH2COOH-C(OH)COOH-CH2COOH·H2O CH2COOH-C(OH)COOH-CH2COOH
Molecular weight 210.14 g/mol 192.12 g/mol
Physical description colorless diamond-shaped crystals colorless, odorless crystals with an acid taste
Melting point 135 °C 153 °C
Solubility freely soluble in water; freely soluble in ethanol; moderately soluble in ether very soluble in water; freely soluble in ethanol; soluble in ether
Density 1.5 g/cm3 1.665 g/cm3
Decomposition 175 °C 175 °C
Anhydrous CA is found in citrus fruits, mahogany and cotton leaves, and wild pomegranates [4][9]. Maintaining a plasma citrate concentration of 100–150 micromoles per liter is vital for various normal physiological processes in humans and animals [10].
CA monohydrate (a food additive E330) is used to enhance the taste, to adjust the acidity, and to improve the efficacy of antimicrobial agents and preservation properties [3][11][12]. CA monohydrate is an ingredient in pharmaceuticals, cosmetics, and fragrances. The reaction of CA with bicarbonates, releasing CO2, is used to improve the solubility of poorly soluble drugs [13]. The composition containing CA is also used to remove metal oxides from the surface of ferrous and non-ferrous metals. CA helps to prevent the boiler fouling [11]). CA is used as a feed additive in agriculture, livestock, and aquaculture [14]. It contributes to the remediation of soil contaminated with heavy metals [12]. CA is also used in electroplating, photography, textiles, etc. [3][9].
Tributyl citrate, the known ester of citric acid, is a safe and non-toxic plasticizer, mostly used in the production of polyvinyl chloride, food films, cellulose resins, synthetic rubber, toys, and flexographic inks. Tributyl citrate is also used as a stabilizer for resins in cosmetics [15].
CA salts are also in great demand in various manufacturing sectors. The most in-demand representative of CA salts is tri-substituted sodium citrate. It is utilized in the chemical, metallurgical, food, medicine, and agriculture industries. It substitutes for hazardous polyphosphates in synthetic detergents, does not corrode metals, and decomposes into carbon dioxide and water in wastewater treatment systems [16][17].
Sodium salts of CA with varying degrees of substitution can be obtained without the need for isolating CA from the culture broth. Titration of the culture broth with NaOH to pH 4.6 produces an equimolar mixture of monosodium citrate and divalent sodium citrate, whereas titration to pH 8.3 yields tri-substituted sodium citrate [18].

3. History

The species Y. lipolytica has approximately twenty synonyms, of which Candida lipolytica is the most prevalent [19].
The yeast C. lipolytica was initially characterized by Harrison in 1928 [9]. Until the discovery of sexual reproduction, this yeast species was classified as an imperfect fungus. Afterward, it was reclassified as a perfect fungus and received various species names. Initially, it was known as Endomycopsis lipolytica (1970), then as Saccharomycopsis lipolytica (1972), and since 1980 as Y. lipolytica [20].
The first publications on the production of CA by C. lipolytica yeast came from Japan and the USSR. Tabuchi et al. (1969) reported that the C. lipolytica No. 228 wild strain could produce 11–34 g/L of CA from glucose, acetic acid, n-butyric acid, oleic acid, fish oil, linseed oil, and soybean oil [21]. This strain prospered from petroleum hydrocarbons, yielding 62.5 g/L of total citric acid from 60 g/L, with a CA/ICA ratio of 2:1 [22]. During that time, Finogenova and colleagues conducted research on the production of organic acids by various strains of C. lipolytica grown on n-alkanes. Their research showed that the growth limitation by mineral components resulted in CA production [23][24][25].
Illarionova and Suetina (1984) [26] noted that there was considerable scientific and practical interest in the production of CA from non-food substrates between 1968 and 1981. The authors reported that 115 patents had been granted for producing CA from n-alkanes using C. lipolytica yeast. The majority of these patents were filed by Japan, the USA, France, Germany, the GDR, and the USSR. Japan’s Kyowa Hakko Kogyo Co. and Taked Chemical Industries LTD were the front-runners in developing CA from n-alkanes.
In the UK, Pfizer played a crucial role in advancing the production of CA. The one-step continuous process with C. lipolytica growing on a mixture of n-paraffins for 304 h was innovative at the time [27].
In France, the Institut Français du Pétrole and the Ecole Nationale Supérieure d’Agronomie et des Industries Alimentaires were responsible for all scientific publications and patents related to the production of CA from n-alkanes [28][29][30].
In the GDR, the Institut für Technische Chemie (Leipzig) carried out the work [31][32].

4. Factors Affecting Citric Acid Production

Y. lipolytica yeast cannot produce citric acid (CA) in a complete nutrient medium. The principal condition of CA overproduction is the limitation of yeast growth by mineral components (nitrogen, phosphorus, sulfur, or magnesium) at a simultaneous excess of a carbon source. As microbial cells require large amounts of nitrogen for growth, the studies are typically conducted using nitrogen limitation. Y. lipolytica yeast produces CA and isocitric acid (ICA) at the same time. The CA/ICA ratio varies depending on the carbon source used. CA is predominantly produced in the medium with glucose and glycerol, while approximately equal amounts of CA and ICA are formed with vegetable oils and n-alkanes. ICA is produced when grown on ethanol. The excretion of CA and ICA into the medium commences only after the exhaustion of nitrogen from the medium, and following the transition of the culture from the logarithmic growth phase to the growth retardation phase. The stationary phase cells remain viable, continuing to synthesize the acids until complete depletion of the carbon source [4][20][33][34][35][36][37][38][39][40].
Y. lipolytica yeast can produce CA from different carbon sources with varying degrees of efficiency. Figure 1 presents the maximal yields (YCA) obtained from different substrates: rapeseed oil [41], n-paraffines [42], sunflower oil [43], raw glycerol [44], extract of Jerusalem artichoke tubers [45], ethanol [46], glucose [47], the mixture of glucose and acetate [48], inulin [49], glucose hydrol [50], the mixture of glucose and oleic acid [51], the mixture of glycerol and olive mills [52], sucrose [53], pure glycerol [54], the mixtue of glucose and olive mills [55], xylose [56], galactose [57], expired “waste” glucose [58], aspen waste [46], grape must [59], carrot juice [60], waste cooking oil [61], fructose [62], the mixture of fructose and whey [59], waste bread hydrolysate [63].These values were found among the wild, mutant, or genetically modified strains of Y. lipolytica.
Processes 11 03435 g001
Figure 1. Maximal citric acid production yields (in g/g) on various carbon sources. The yields are displayed at the top of the bars.
Y. lipolytica yeast gives maximum yields from n-paraffins (1.44 g/g) [42] and vegetable oils (1.42–1.5 g/g) [41][43]. High yields can be obtained using glucose (0.86 g/g) [47] and ethanol (0.87 g/g) [46] as carbon sources. Y. lipolytica yeast can utilize industrial waste. For instance, the mutant strain Y. lipolytica NG40/UV7 can produce CA with a yield of 0.95 g/g from glycerol-containing waste from the biodiesel industry [44].
Y. lipolytica yeast can utilize plant sources and waste from the food industry. For instance, the mutant strain of Y. lipolytica A-101-1.14 can produce CA with a yield of 0.95 g/g from starch-derived glucose hydrol [50]. The wild strain Y. lipolytica ACA-YC 5033 can utilize the combination of olive mill wastewater with glucose or glycerol and produce CA with a yield of 0.63–0.69 g/g [52][55]. Ra et al. [45] achieved a yield of 0.91 g/g using Jerusalem artichoke tuber extract. Recombinant strains of Y. lipolytica can utilize sucrose [53][64] and inulin [49]. Y. lipolytica can use aspen waste [46], xylose [56], galactose [57], fructose [62], whey [59], grape must [59], carrot juice [60], waste cooking oil [61], waste bread hydrolysate [63], sunflower waste cooking oil [65], and straw hydrolysate [66]. Diamantopoulou et al. [58] converted the expired “waste” glucose to CA with a yield of 0.5 g/g. Promising carbon sources for large-scale CA production include low-cost corn syrups and corn steep liquor derived from the saccharification of corn starch [67][68]. Gao et al. [69] used corn stover treated with glycerol-assisted instantaneous catapult steam explosion to produce CA and mannitol. Although industrial and agricultural wastes are affordable carbon sources, making them economically preferable raw materials, their processing is challenging and arduous. These wastes can contain trace metals that can inhibit yeast growth and CA synthesis. Researchers often employ chemical pretreatment of substrates and use distilled water instead of tap water when working with waste materials [36].
High yields can be obtained using a dual-substrate medium. Venter et al. [70] found that acetate enhanced CA production; its addition to sunflower oil resulted in a 37-fold increase in CA production and a 2-fold increase in the CA/ICA ratio in Y. lipolytica UOFS Y-1701. Robak et al. [48] found that the addition of acetate to the glucose medium improved the specific production rate, yield, and productivity of CA biosynthesis by Y. lipolytica.
It should be noted that studies comparing the effect of different carbon sources on citrate production are limited. Rywinska et al. [71] found that pure glycerol was a superior substrate compared with crude glycerol and glucose. Celik et al. [72] reported that sunflower oil was superior to glucose and glycerol. When comparing rapeseed oil, glucose, glycerol, ethanol, glycerol-containing biodiesel industry waste, and glucose-containing aspen waste, it was shown that rapeseed oil, ethanol, and crude glycerol allowed high CA production (100–140 g/L), whereas aspen waste resulted in a low CA concentration (31.2 g/L) [46].
The choice of the optimum initial carbon source concentration depends on the strain, the composition of the nutrient medium, and the cultivation conditions. Usually, the optimal yields are obtained at initial carbon concentrations of 50–250 g/L [73], with the exception of ethanol (0.1–1.0 g/L) [46].
Y. lipolytica yeast requires nitrogen, phosphorus, sulfur, potassium, magnesium, calcium, and trace elements in its nutrient medium. The ideal dosage of these elements is dependent on the physiological characteristics of the strain and the carbon source [36][73].
Y. lipolytica yeast can use both inorganic salts, such as NH4Cl and (NH4)2SO4, and organic compounds, such as yeast extract and peptone, as nitrogen sources for CA production. It is crucial to select an appropriate nitrogen concentration that guarantees enough cell density in the culture medium. In general, Y. lipolytica yeast grown on pure substrates such as glucose and glycerol requires between 630 and 1200 mg/L of nitrogen [73]. Kamzolova et al. [74] found that the volumetric productivity (QCA) was very high (1.11 g/L·h) at a nitrogen concentration of 1200 mg/L. However, waste with a high nitrogen content can be utilized without adding nitrogen to the medium. Ra et al. [45] reported that CA production from Jerusalem artichoke tuber extract requires no nitrogen source. Moreover, Carsanba et al. [63] observed similar results with waste bread hydrolysate. Da Silva et al. [75] showed that the addition of ammonium sulfate to the culture medium shifts the metabolic pathway to isocitrate acid production in Y. lipolytica grown on crude glycerol. However, it was necessary to add nitrogen and magnesium to accumulate CA from waste cooking oil [61].
The carbon-to-nitrogen (C/N) ratio plays a critical role in the regulation of CA biosynthesis. Carsanba et al. [76] studied the effect of initial C/N ratios (167, 367, and 567) on CA production by Y. lipolytica K57 grown on glucose. The best C/N ratio was found to be 367, which resulted in the highest CA concentration, yield (YCA), and CA production rate (qCA). Levinson et al. [77] found that the best CA/ICA ratios in Y. lipolytica grown on glycerol were achieved between C/N ratios of 343 and 686. Another study found that Y. lipolytica W29 could produce CA from high fructose syrup at a C/N mass ratio of 75, but, after 15 days at a C/N ratio of 150, CA production stopped while lipid accumulation increased [68].
Y. lipolytica yeast uses KH2PO4, K2HPO4, and Na2HPO4 as sources of potassium and phosphorus. The concentrations vary from 100 to 2400 mg/L [33][48][74][75].
For intensive production of CA, Y. lipolytica yeast require specific microelements. These microelements can either activate or inhibit enzymes involved in the metabolism of Y. lipolytica. To activate alcohol dehydrogenase when Y. lipolytica is grown on ethanol, it is necessary to maintain a Zn2+ concentration of at least 1 mg/g of cells [78]. Y. lipolytica also requires iron. Under iron deficiency, most of the acetyl-CoA does not participate in the TCA cycle but undergoes condensation to form ethyl acetate [79]. In contrast, the increased iron concentration leads to activation of the TCA cycle, respiratory chain, and oxidative phosphorylation in Y. lipolytica [80]. However, the substantial increase in Fe2+ ion concentration has minimal effect on yeast growth and total amounts of acids. But, it alters the balance between these acids, favoring the formation of ICA [81][82]. The positive effect of copper ions on the metabolism of Y. lipolytica is well studied. The addition of 2.5–5 mg/L Cu2+ to Y. lipolytica yeast grown on glycerol leads to increased production of erythritol, CA, and α-ketoglutaric acid [83]. In addition, CA production is stimulated by Mn2+ [84]. Researchers often use tap water rather than a microelement solution [48][53][56][85].
Y. lipolytica is unable to synthesize the thiamine molecule, i.e., the pyrimidine moiety, and requires thiamine to be added to the medium. In the absence of thiamine, the yeast produces pyruvic acid and α-ketoglutaric acid rather than CA [86][87][88][89][90][91]. A sufficient quantity of thiamine (100–200 µg/L) should be added to the growth medium. Yeast extract can replace thiamine [86][87][88][89][90][91]. However, an excessive amount is not recommended because nitrogen is also present, not just vitamins.
Information regarding the impact of growth temperature on CA production is limited. Morgunov et al. [54] found that Y. lipolytica grown on glycerol exhibited optimal CA production at temperatures between 28 and 30 °C, with the yield declining even if the cultivation temperature shifted by just 2 °C in either direction. Moeller et al. [92] determined that Y. lipolytica growth was ideal within the 30–34 °C temperature range. However, it was found that CA production reached its maximum levels only at 30 °C. Arslan et al. [93] introduced the Y. lipolytica B9 strain that is adapted to low temperatures. This strain successfully produced 33.3 g/L of CA, even at 20 °C.
The pH medium level is a critical factor affecting Y. lipolytica yeast metabolism. Yeast grows at pH values between 2.5 and 11.5, although CA production only occurs within a pH range of 4.5 to 6.0 [73]. Zhang et al. [94] found that the wild strain Y. lipolytica W 29 produced CA at a neutral pH while generating lipids at an acidic pH. The authors have proposed that this pH-dependent mechanism is impacted by CA transport, rather than alterations in enzyme expression for acid production and lipid synthesis. Gao et al. [69] found the shift from CA production at pH 5.5 to mannitol synthesis at pH 3.5 in Y. lipolytica CGMCC 2.1506 yeast grown on corn stover enzymatic hydrolysate. Another strain, Y. lipolytica H222, grown on glycerol, simultaneously produced CA (19.1 g/L), mannitol (18.1 g/L), arabidol (2.3 g/L), and erythritol (6.7 g/L) at pH 3.5, but at pH 5.5 it produced 42.5 g/L CA without polyol accumulation [95]. In spite of this, some genetically modified strains have a higher pH tolerance. Mirończuk et al. [96] found that strains overexpressing GUT1 and/or GUT2 have the ability to produce substantial amounts of CA from glycerol at pH 3. This capability to synthesize metabolites at a low pH has significant industrial value since it reduces production costs, prevents bacterial contamination, and maintains aseptic conditions. Another genetically modified strain exhibited higher invertase at a pH range of 6.0–6.8, thus increasing the production of CA from sucrose to 127–140 g/L. However, at a pH of 5.0, the yield dropped to 87 g/L [64].
The production of CA by Y. lipolytica yeast is affected by aeration, namely the oxygen saturation level (pO2) in the culture medium. The appropriate pO2 level is dependent upon the carbon source. For the biosynthesis of CA from n-paraffins, it is necessary to maintain optimum pO2 levels between 70 and 90% saturation [23]. To promote CA production from vegetable oils and ethanol, it is essential to maintain high levels of aeration, typically at 50–60% saturation [41][97]. In order to achieve the highest levels of CA production using other carbon sources, it is important to maintain a minimum pO2 value of 20% saturation [72]. Liu et al. [51] recommended increasing the oxygen saturation level by introducing oxygen vectors such as oleic acid. Bellou et al. [98] noted that the pO2 value, rather than the type of carbon source or the nitrogen concentration in the medium, had an effect on the morphology of Y. lipolytica. Their research showed that, at low or zero pO2, mycelial and/or pseudomycelial forms were more prevalent than yeast-like forms. Another important oxygenation factor is the initial volumetric oxygen mass transfer coefficient (kLa), which is sensitive to operating conditions such as stirring speed, specific air flow rate, and cell density. Ferreira et al. [99] showed a 7.8-fold increase in CA production by increasing the initial kLa from 7 h−1 to 55 h−1.
Different types of bioreactors have been constructed to obtain an adequate volumetric oxygen mass transfer coefficient without high aeration rates. These bioreactors can provide significant cost savings during operations. It was observed that, using airlift and pressurized bioreactors, Y. lipolytica W29 could produce 14 g/L and 6 g/L of CA, respectively [100].
In summary, the essential conditions for CA synthesis by the Y. lipolytica yeast include nitrogen limitation, carbon excess, temperature control between 28 and 30 °C, pH control of the medium to about 4.5 to 5.5, and adequate aeration.

5. Wild-Type CA Producers

Table 2 presents efficient methods for the production of citric acid (CA) by well-known wild strains of Y. lipolytica. The strains under consideration were sourced from various countries, including Poland (A-101), the United States (ATCC 76598, ATCC 8661, and ATCC 20346), China (SWJ-1b), Germany (H 222, DSM 8218, and DSM 3286), Greece (ACA-DC 50109 [LGAM S(7)1], ACA-DC 5031, ACA-DC 5033, LMBF-46), France (W29), Russia (VKM Y-2373), and Turkey (K 57).
Table 2. Citric acid production by wild strains of Y. lipolytica.
Strain Isolation Source Carbon Source CA
(g/L)		 Selectivity
(%)		 YCA
(g/g)		 QCA (g/L·h) Culture Mode Ref.
A-101 oil-field, Poland n-hexadecane n.d. 54–64 1.44 n.d. batch [42]
glucose 69.3 83 0.45 0.85 batch [71]
glycerol 66.5 78.9 0.44 0.65 batch [71]
crude glycerol 66.8 84.3 0.43 0.80 batch [71]
glucose hydrol 91.4 95.0 0.67 1.01 batch [50]
ACA-DC 50109 [LGAM S(7)1 Greece glucose 42.9 n.d. 0.56 n.d. flask [101]
crude glycerol 35.1 n.d. 0.42 n.d. flask [102]
OMW + crude glycerol 30.3 n.d. 0.62 0.11 flask [103]
OMW + glucose 28.9 n.d. 0.53 n.d. flask [104]
expired “waste” glucose 82.0 n.d. 0.50 n.d. FB [58]
ACA-DC 5029 Greece crude glycerol 39 n.d. 0.42 n.d. batch [105]
OMW + crude glycerol 79.0 n.d. 0.39 n.d. batch [106]
ACA-DC 5031 wheat, Greece OMW + glucose 52.0 n.d. 0.64 n.d. flask [107]
ACA-YC 5033 Greece glucose 18.9 n.d. 0.49 0.113 flask [55]
OMW + glucose 25.8 n.d. 0.63 0.215 flask [55]
D 1805 USA glucose 69.5 n.d. 0.47 n.d. recycle [108]
DSM 3286 Germany glucose 35 n.d.   n.d. flask [109]
glucose 75.0 n.d. 0.80 n.d. batch [110]
DSM 8218 diesel tank, Germany crude glycerol n.d. n.d. 0.53 n.d. batch [111]
H222 soil, Germany glucose 62.5 91 0.37 1.48 batch [112]
glucose 132.6 89 0.67 0.78 FB [112]
glucose 66.5 92 0.48 1.70 RB [112]
glucose 100.0 92 0.65 1.14 RFB [112]
glycerol 42.5 88.9 0.48   batch [95]
K57 Turkey glucose 72.12 n.d. 0.77 0.39 batch [76]
fructose 65.1 n.d. 0.38 0.283 batch [62]
whey + fructose 49.23 n.d. 0.33 n.d. batch [59]
grape must 32.09 n.d. 0.48 n.d. batch [59]
waste bread hydrolysate 15 n.d. 0.11 0.30 batch [63]
LMBF Y-46 Greece glycerol 42.4 n.d. 0.41 n.d. batch [113]
glycerol 101.3 n.d. 0.46 n.d. FB [113]
OMW + crude glycerol 64.1 n.d. 0.682 0.335 flasks [52]
NRRL Y-7576 USA glucose 75 n.d. 0.86 1.16 recycle [47]
NRRL Y-1095 USA glucose 22 0.45–0.72 0.65 1.32 recycle, FB [114]
SWJ-1b the gut of the marine fish of Bohai Sea, China glucose 25.9 82 * 0.60 0.117 * flask [51]
glucose + oleic acid 33.2 84 * 0.73 0.161 * flask [51]
glucose + CSL 52.3 91 * 0.87 * 0.22 batch [67]
hydrolysate of straw 26.7 66 * n.d. n.d. batch [66]
hydrolysate of straw 42.4 91 * n.d. n.d. FB [66]
waste cooking oil 31.7 83 * 0.4 n.d. FB [66]
W 29 sewage, France n-paraffines 92.0 65.2 0.38 * n.d. batch [30]
glucose 106.7 91.2 0.44 * n.d. batch [30]
glucose 49 n.d. 0.85 n.d. flask [115]
OMW + glucose 15.8 n.d. 0.46 n.d. flask [116]
glycerol 125.5 91.7 0.52 * n.d. batch [30]
crude glycerol 81.11 n.d. n.d. n.d. batch [117]
crude glycerol 14.0 n.d. 0.40 n.d. airlift [100]
crude glycerol 6.0 n.d. 0.32 n.d. pressurized [100]
VKM Y-2373 Russia glucose 99.9 n.d. 0.77 0.86 FB [74]
crude glycerol 67.7 n.d. 0.59 0.55 FB [44]
*—Calculated according to presented data; n.d.—not determined; OMW—olive mill waste water; CSL—corn steep liquor; FB fed-batch; RB—repeated batch; RFB—repeated fed batch.
Wild-type strains of Y. lipolytica exhibit their universal capability to produce CA through various carbon sources and cultivation techniques, such as flask, batch, fed-batch, repeated-batch, and repeated-fed-batch. For instance, the wild strain Y. lipolytica A-101 from Poland can produce over 65 g/L of CA from glucose and glycerol [71], and more than 90 g/L of CA from glucose hydrolysates [50] in batch mode.
The wild strain Y. lipolytica ACA-DC 50109 (Y. lipolytica LGAM S(7)1), selected at the Laboratory of General and Agricultural Microbiology of the Agricultural University of Athens, was one of the first strains to be investigated for its ability to produce CA from biodiesel waste. This strain can produce 35.1 g/L CA with a yield of 0.42 g/g on crude glycerol [102]. The strain Y. lipolytica LGAM S(7)1 can produce 82 g/L CA with a yield of 0.50 g/g from expired “waste” glucose [58]. Additionally, this strain was tested with a mixture of crude glycerol and olive mill effluent—an agro-industrial waste known for its difficulty in processing. The purpose of this experiment was to reduce the potential of the crude glycerol by blending it with the olive mill effluent and replacing some or all of the tap water used in the process. By using two substrates, the Y. lipolytica LGAM S(7)1 yeast produced 30.3 g/L CA with a yield (YCA) of 0.62 g/g in flasks [103]. Later, the authors enhanced the CA production process up to 52.0 g/L, with a yield (YCA) of 0.64 g/g, using another wild strain, Y. lipolytica ACA-YC 5033. This strain effectively eliminated the noxious phenolic compounds from olive mill wastewater (around 51% in weight) [107]. Another strain, Y. lipolytica ACA-DC 5029, grew well on a mixture of crude glycerol and olive mill effluent and produced up to 79.0 g/L CA with a yield (YCA) of ~0.46 g/g, but accumulated erythritol in significant amounts (66.0 g/L) [106].
The French wild strain Y. lipolytica W29 can produce more than 100 g/L CA from glucose and glycerol [30]. In addition to these carbon sources, Y. lipolytica W29 produced CA from untreated crude glycerol [117], as well as from inexpensive, year-round nutrient sources obtained during the corn wet milling process, such as food-grade corn syrups and corn steep liquor [68]. However, when cultivated in glucose-enriched olive mill wastewater, the strain produced only 15.8 g/L CA with a yield (YCA) of 0.46 g/g [116]. Using this particular strain, it was shown that the control of reactive oxygen species, particularly via alternative oxidase activity, is essential for regulating the balance between citrate and lipid fluxes [118].
The wild strain Y. lipolytica H222 from Germany has served as the foundation for creating certain recombinant strains that overproduce CA. Furthermore, it is an invaluable model for evaluating the impact of various cultivation methods on CA biosynthesis. Moeller et al. (2010) examined CA biosynthesis in batch, fed-batch, repeated batch, and repeated fed-batch using the aforementioned strain [112]. The authors showed that using a repeated fed-batch process with Y. lipolytica H222 grown on glucose gave the best results. In each 72 h cycle, 100 g/L of CA was produced, with a yield (YCA) ranging from 0.51 to 0.65 g/g and a selectivity of 94%. The repeated fed-batch mode allowed for a 32% increase in CA production compared with batch fermentation.
The wild strain Y. lipolytica K 57, selected at the Department of Food Technology, Faculty of Engineering, University of Ankara (Turkey), is recognized as one of the leading producers of CA in fructose, whey, and grape must media [59][62].
Researchers use the wild strain Y. lipolytica 704 (Y. lipolytica VKM Y-2373) in their study. This strain was originally obtained in 1963 from activated sludge from the Angarsk oil refinery effluent treatment plant in the USSR. It can produce significant amounts of CA from crude glycerol [44] and glucose [74]. The biomass, a by-product of CA production, possesses a significant quantity of essential amino acids and unsaturated fatty acids, making it suitable for application in the areas of food biotechnology and agriculture [74].
In recent years, there have been reports of various pioneering strains that produce considerable amounts of CA. One such strain is the wild strain Y. lipolytica LMBF Y-46, which was isolated from gilt-head (sea) bream (Sparus aurata) fish and cultivated with glycerol. This strain achieved over 100 g/L CA, which is among the highest reported values [113]. Moreover, in Germany, the novel strain Y. lipolytica DSM 8218 was isolated from a diesel tank. This microbe can grow on fuel, so its suitability for growth on crude glycerol, containing microbial inhibitors and diesel production residues, should be investigated. This particular strain showed a faster growth rate on impure glycerol than on pure glycerol due to its consumption of acetic acid as a secondary substrate [111].
There are a number of publications on wild strains of Y. lipolytica D 1805, Y. lipolytica NRRL Y-7576, and Y. lipolytica NRRL Y-1095 that are able to promote active acid production during long-term cultivation (500–700 h) [47][108][114].
It should be noted that wild strains of Y. lipolytica produce CA and ICA simultaneously in virtually all carbon sources studied. This has led research teams to focus on the development of strains with predominant CA production.

6. Mutagenesis and Selection

Many research teams used physical and chemical mutagens to produce mutant strains with increased CA synthesis and decreased ICA content. Exposure to UV radiation leads to the excitation of electrons in DNA molecules, resulting in the creation of additional bonds between adjacent pyrimidine bases on one or both chains of DNA, thus forming dimers. This process causes transitions, transversions, frame shifts, and deletions. UV radiation has a wavelength range of 200–400 nm. N-methyl-N-nitro-N-nitrosoguanidine (NTG) and N-nitroso-N-methylurea (NMM) are common chemical mutagens. They induce alkylation and oxidation of nucleotide bases. This leads to mutations [9].
The conventional method of selecting mutant CA producers generally involves the following steps [119]:
(1)
Isolation of monoclones from the parent strain;
(2)
Treatment of clones by physical action or chemical mutagen;
(3)
Streaking of treated clones on agar plates and selection of variants weakly growing on citrate (Cit−) or acetate (Ace−);
(4)
Evaluation of the acid-forming activity of the Cit− or Ace− variants by zones of dissolution of chalk on agar medium;
(5)
Cultivation of the selected variants under standard conditions on liquid medium and selection of the most active mutant strain;
(6)
Conservation of the active mutant strain of CA production.
Table 3 presents efficient methods for the production of CA by well-known mutant strains of Y. lipolytica.
Table 3. Citric acid production by mutant strains of Y. lipolytica.
Mutant Strain Parental Strain Mutagen/Screening Carbon Source CA
(g/L)		 Selectivity
(%)		 YCA (g/g) QCA (g/L·h) Culture Mode Ref.
Wratislavia 1.31 (A-101.1.31) A-101 UV/Ace− glucose 76.4 93.2 0.48 0.76 batch [71]
glycerol 82 96 0.53 0.79 batch [71]
crude glycerol 124.5 97 * 0.62 0.88 batch [120]
A-101-1.14 A-101 UV/Cit− glucose hydrol 94 94 0.85 1.25 batch [50]
AWG7 Wratislavia 1.31 UV/Ace− glucose 78.5 95.7 0.52 0.76 batch [71]
glycerol 82.9 96.4 0.53 0.66 batch [71]
crude glycerol 88.1 95 * 0.46 0.91 batch [120]
glycerol 97.8 n.d. 0.49 0.98 chemostat [121]
crude glycerol 154 n.d. 0.78 1.05 RB [122]
Wratislavia K1 Wratislavia 1.31 chemostat glucose 49.5 91.2 0.30 0.65 batch [71]
glycerol 53.3 95.2 0.34 0.58 batch [71]
crude glycerol 75.7 95 * 0.40 0.81 batch [120]
A-101-1.22 A-101 NTG/Ace− glucose hydrol 78.1 88 0.60 0.71 batch [50]
crude glycerol 112 94 * 0.6 0.71 batch [123]
crude glycerol 96–107 94 * 0.64 1.42 recycle [123]
crude glycerol 124.2 95 * 0.77 0.85 RB [123]
K-20 ATCC20114 NTG/Cit− n-paraffins 91.0 85 1.45 n.d. batch [124]
S-22 ATCC20114 NTG/fluoroacetate-sensitive n-paraffins 106.0 97 1.45 n.d. batch [124]
BAFC 3852 NRRL Y-1095 NTG glycerol 32.1 n.d. 0.22 n.d. flask [68]
NTG9 ATCC 20228 NTG canola oil 137.5 n.d. 0.49 n.d. FB [84]
VKPM Y-184 704 NMM/Cit- n-paraffins 217.0 97 1.45 n.d. batch [2]
N 1 704 NMM/Cit- ethanol 120 n.d. 0.87 1.15 FB [97]
NG40/UV7 Y. lipolytica 704 NTG/UV/Ace− rapeseed oil 175 97 1.5 1.34 FB [42]
glucose 100.8 95 0.8 1.05 FB [54]
glycerol 115 96 0.64 0.906 FB [54]
ethanol 106.7 88 0.87 1.32 FB [54]
crude glycerol 122 98 * 0.95 0.99 FB [54]
K168 57 EMS glucose 50.1 n.d. n.d. 0.214 FB [125]
carrot juice 80.53 n.d. 0.42 0.374 FB [60]
*—Calculated according to presented data; n.d.—not determined; Ace−—variants weakly growing on acetate; Cit−—variants weakly growing on citrate; EMS—ethyl methane sulfonate; FB—fed-batch; RB—repeated batch; NMM—N-nitroso-N-methylurea; NTG—N-methyl-N-nitro-N-nitrosoguanidine; UV—UV radiation.
The first mutants with minimal amounts of ICA in n-paraffin medium were obtained in Japan. A wild strain of C. lipolytica ATCC20114 was treated with NTG (250 µg/mL) for thirty minutes. The mutant variants were then screened for lack of growth in citrate media or sensitivity to fluoroacetate. The use of fluoroacetate is necessary because it inhibits the TCA cycle. Fluoroacetate undergoes enzymatic conversion to the toxic metabolite fluorocitrate, which inhibits aconitase and shifts the metabolism towards predominantly synthesizing CA. Two mutants were selected: K-20 (unable to grow on citrate), which produced 91 g/L CA with a selectivity of 85%, and the fluoroacetate-sensitive mutant S-22, which produced 106 g/L CA with a selectivity of 97%. In contrast, the parental strain C. lipolytica ATCC20114 can produce CA with low selectivity (60%) [124].
The Polish team successfully generated a series of effective mutants by exposing the wild strain Y. lipolytica A-101 to UV irradiation and NTG. The positive variants were selected by their inability to grow on media containing acetate (Wratislavia 1.31, AWG7, A-101.-1.22) or citrate (A-101.-1.14) and by prolonged cultivation in a chemostat. These mutants have the ability to produce CA from different carbon sources. For example, the UV citrate-negative mutant Y. lipolytica A-101-1.14 can produce 94 g/L of CA from glucose hydrolysates with a selectivity of 94%, a product yield (YCA) of 0.85 g/g, and a productivity (QCA) of 1.25 g/L·h [50]. In addition, the mutants show remarkable stability during continuous cultivation. For example, the double UV acetate-negative mutant Wratislavia AWG7 grown on glycerol can produce 97.8 g/L CA with a yield (YCA) of 0.49 g/g and a productivity (QCA) of 0.98 g/L·h for 550 h in the chemostat (using a dilution rate of 0.01 h−1) [121]. A more efficient approach using the 40% repeated batch mode was also developed: the mutant Wratislavia AWG7 produced 154 g/L CA with a product yield (YCA) of 0.78 g/g and a productivity (QCA) of 1.05 g/L·h. The activity of the mutant remained stable for more than 1650 h [122]. These mutants are maintained in the yeast culture collection of the Department of Biotechnology and Food Microbiology, Wroclaw University of Environmental and Life Sciences in Poland.
A highly efficient mutant of C. lipolytica VKPM Y-184 was obtained through exposure of the wild strain Y. lipolytica 704 to NMM. The mutant can produce 217 g/L CA with a selectivity of 97% and yield (YCA) of 1.45 g/g [4].
The mutant strain Y. lipolytica BAFC 3852, obtained through exposure of the wild strain Y. lipolytica NRRL Y-1095 to NTG, lacks the ability to form true mycelium or pseudomycelium, but forms only yeast-like cells. This attribute results in better stirring of the nutritional medium in the bioreactor, thus improving the overall process. This mutant produces 32.1 g/L CA from corn wet milling products [68].
The mutant strain Y. lipolytica N 1, obtained by exposing the wild strain Y. lipolytica 704 to NMM, can produce 120 g/L of CA with a yield (YCA) of 0.87 g/g from ethanol, even under low aeration (pO2 = 20% of saturation) [97]. However, it is required to use an iron-enriched medium to achieve these results.
The combination of chemical mutagens and UV radiation produces remarkable results. For example, the double mutant Y. lipolytica NG40/UV7 shows an impressive ability to produce significant amounts of CA while minimizing ICA levels on a variety of carbon sources. This mutant can produce 175 g/L of CA on rapeseed oil [41], 115 g/L on glycerol [54], and 122.2 g/L on crude glycerol [44].

7. Metabolic Engineering

In recent years, rational metabolic engineering has gradually replaced traditional mutagenesis as a powerful approach to improve strains and processes for CA production. Strategies include activation of key metabolic pathways for assimilation of carbon sources, CA biosynthesis, and its precursors; and inactivation of by-product synthesis pathways and pathways for CA degradation or its involvement in further transformations. A schematic overview of the metabolic pathways of citric acid production from different carbon sources, including well-known sources such as n-alkanes, triglycerides, fatty acids, glucose, glycerol, and fructose, as well as less-studied sources such as galactose, xylose, and inulin, can be found in recent reviews [34][36][37][126][127]. Therefore, only genetic techniques that demonstrate significant effectiveness in CA production by Y. lipolytica are presented in this section.
Table 4 presents efficient methods for the production of CA by well-known genetically modified strains of Y. lipolytica.
Table 4. Citric acid production by genetically modified strains of Y. lipolytica.
Transformant Parental Strain Metabolic
Strategy		 Carbon Source CA
(g/L)		 Selectivity
(%)		 YCA (g/g) QCA (g/L·h) Culture Mode Ref.
CIT1 A-101 YlCIT1 rapeseed oil 67.8 49 0.34 0.36 batch [128]
CIT2 A-101 YlCIT2 rapeseed oil 53.6 51 0.22 0.28 batch [128]
AJDpADUTGut1/2 A101 YlGUT1, YlGUT2 glycerol 92.9 n.d. 0.62 1.29 batch,
pH = 6		 [96]
crude glycerol 33.4 * n.d. 0.23 * n.d. batch,
pH = 3		 [129]
A101-B56-5 A-101 ScSUC2 sucrose 58.83 99 0.65 0.82 batch [53]
CIT1 Wratislavia 1.31 YlCIT1 glycerol 60.33 72 0.39 0.42 batch [128]
CIT2 Wratislavia 1.31 YlCIT2 glycerol 73.96 82 0.43 0.53 batch [128]
H222-S4(p67ICL1) T5 H222 YlICL1 glucose n.d. 96–98 n.d. n.d. flasks [130]
sunflower oil n.d. 93 n.d. n.d. flasks [130]
H222-41(JMP5)Z1233 H222 Δicl1 glucose n.d. 80 n.d. n.d. flasks [130]
H222-S4(p67ICL1) T5 H222 ScSUC2, YlICL1 sucrose 140 96 0.82 0.73 FB [64]
sucrose 57.7–114.5
114.5		 93.7–96.4 0.49–0.64 0.66–1.0 RB [131]
PG86 SWJ-1b MgPYC glucose 101.0 66 * 0.89 0.43 FB [132]
PR32 SWJ-1b PrPYC1 glucose 111.1 62 * 0.93 0.46 FB [133]
No. 87 SWJ-1b KmSUC2 inulin 68.9 94 * 0.69 0.22 flasks [134]
AWG7 INU 8 SWJ-1b KmSUC2 inulin 203 n.d. 0.85 0.51 RB [49]
No. 30 SWJ-1b KmSUC2, YLICL1, Δacl1 inulin 84 98 * 0.84 * 0.39 * batch [135]
extract of Jerusalem artichoke tubers 68.3 n.d. 0.91 n.d. batch [45]
XYL+ W29 SsXR, SsXDH,
YlXK		 xylose 79.4 n.d. 0.53 0.91 batch [56]
Y4588 W29 YlGAL1, YlGAL7, YlGAL10E, YlGAL10M galactose 29.2 n.d. 0.51 n.d. batch [57]
Transformant W29 YlYHM2, YlAMPD glucose 97.1 94 * 0.5 0.8 FB [136]
JMY1203 W29 Δphd1 crude glycerol 57.7 >95 0.91 n.d. flasks [137]
*—Calculated according to presented data; n.d.—not determined.
Y. lipolytica yeast is unable to assimilate sucrose as it lacks the enzyme invertase, which is necessary for the hydrolysis of sucrose into glucose and fructose. To address this, recombinant strains of Y. lipolytica were created, which overexpress the SUC2 gene encoding invertase. The recombinant strain Y. lipolytica A101-B56-5, which overexpresses the SUC2 gene from Saccharomyces cerevisiae, exhibited strong growth on sucrose and produced 58.83 g/L CA with a yield (YCA) of 0.65 g/g and a productivity (QCA) of 0.82 g/L·h. Meanwhile, the ICA content was very low (1.26%) [53].
Given the problem of glucose preference, efforts have been made to develop strains that can use both fructose and glucose simultaneously. Expression of the HXK1 gene, which encodes the hexokinase enzyme responsible for fructose phosphorylation, improved fructose utilization, reduces filament formation, and increases CA synthesis [138]. Furthermore, simultaneous expression of the HXK1 gene with the hexose transporter genes Yht1 and Yht6 significantly increased CA production [139].
Recombinant strains that can grow on inulin have been developed. For instance, based on Y. lipolytica SWJ-1b, a recombinant strain was constructed in which the INU1 gene from Kluyveromyces marxianus encoding an extracellular inulinase was expressed. This strain can produce 68.9 g/L CA with a yield (YCA) of 0.69 g/g and a productivity (QCA) of 0.22 g/L·h [134].
To enhance glycerol assimilation, the expression of glycerol-assimilating enzymes, namely glycerol kinase encoded by GUT1 and glycerol-3P-dehydrogenase encoded by GUT2, is necessary. Overexpression of GUT1 significantly increases glycerol assimilation, while a strain with the GUT2 gene expression showed increased CA production [96]. The authors note that GUT2 is crucial for CA production, as the carbon flux in the cell is redirected to the TCA cycle. Recombinant strains with GUT1 and GUT2 exhibit metabolic lability: when grown in glycerol medium, the transformant Y. lipolytica AJD pADUTGut1/2 can produce 92.9 g/L CA at pH 6.0, but, at pH 3, the metabolism shifts towards erythritol accumulation (78 g/L) rather than CA. Rzechonek et al. [129] revealed that transformant Y. lipolytica AJD pADUTGut1/2 can produce CA at pH 3 in aseptic conditions using crude glycerol.
Recently, the rapid development of the CRISPR/Cas9 system has facilitated highly efficient genomic genetic editing in Y. lipolytica. New GoldenMOCS plasmids are appropriate for extrachromosomal overexpression of the GUT1 gene in wild-type strains of Y. lipolytica, resulting in an elevated conversion of glycerol to erythritol and CA [140].
It should be noted that wild strains of the yeast Y. lipolytica cannot grow on galactose. However, a modified Y. lipolytica Y4588 strain that overexpresses four genes encoding Leloir pathway enzymes (galactokinase, galactose-1-P-uridyl transferase, UDP-glucose-4-epimerase, and galactose mutarotase), YlGAL1, YlGAL7, YlGAL10E, and YlGAL10M, can assimilate galactose and produce 29.2 g/L CA with a yield (YCA) of 0.51 g/g, which is comparable to glucose [57].
In medium with xylose, the Y. lipolytica XYL+ transformant, overexpressing the xylose reductase-encoding gene XR and xylitol dehydrogenase-encoding gene XDH from Scheersomyces stipites in addition to the endogenous xylulokinase-encoding gene XK, produced 79.4 g/L CA with a yield (YCA) of 0.53 g/g and a productivity (QCA) of 0.91 g/L·h [56].
Acetyl-CoA and oxaloacetate are two direct substrates for CA synthesis. A number of papers have been devoted to recombinant strains overexpressing the PYC gene encoding pyruvate carboxylase, which converts carboxylate pyruvate to oxaloacetate. A recombinant transformant PG86, harboring a pyruvate carboxylase-encoding PYC gene from Meyerozyma guilliermondii, can produce 101 g/L CA with a yield (YCA) of 0.89 g/g and a productivity (QCA) of 0.42 g/L·h from 120 g/L glucose within 240 h of the fed-batch fermentation. Nonetheless, the by-product content was high, reaching 34.4 g/L, of which 12.4% constituted malate [132]. Another transformant PR32 harboring a pyruvate carboxylase-encoding PYC gene from the marine fungus Penicillium rubens exhibited an 8-fold increase in pyruvate carboxylase activity and a 2.6-fold higher acid-forming capacity. When cultivated in a fed-batch mode using glucose medium, the transformant PR 32 produced 111.1 g/L of CA with a yield (YCA) of 0.93 g/g and a productivity (QCA) of 0.46 g/L·h. However, the by-product content was quite high, at 38.1 g/L, including malate at 10.1% [133].
Biochemical studies indicate that citrate biosynthesis is determined by the high activity of citrate synthase compared with subsequent enzymes [42][54]. However, a recombinant strain, obtained from mutant Wratislavia, overexpressing the CIT 1 and CIT 2 genes encoding citrate synthase had no effect on citrate biosynthesis on glycerol, but caused a 10% and 23% increase in total acid biosynthesis compared with the parental strain, as a consequence of increased isocitrate synthesis [128]. The CIT1 and CIT2 mutants, obtained from the wild strain Y. lipolytica A-101, also did not show increased citrate biosynthesis but produced significant amounts of ICA (approximately 60 g/L) on rapeseed oil [128].
Strains that expressed multicopies of isocitrate lyase demonstrated a more favorable CA to ICA ratio compared with the wild type. The ICA percentage decreased from 10–12% to 3–6% in medium containing glycerol, glucose, and sucrose. In medium containing sunflower oil or hexadecane, the percentage of ICA was reduced from 37–45% to 4–7%. However, the transformant did not impact the overall concentration of citric acids [130]. In contrast, the defective strain Y. lipolytica H222-41(JMP5) Z123 exhibited a 2–5% increase in the proportion of isocitric acid compared with the wild strain Y. lipolytica H222 when grown on glucose or glycerol due to the lack of isocitrate lyase activity [130]. Another transformant, Y. lipolytica H222-S4(p67ICL1) T5, that overexpressed SUC2 and ICL1 produced 140 g/L CA on sucrose with a low ICA content (4%) at pH = 6.8 [64]. The strain was subsequently assessed through repeated fed-batch and fed-batch modes for over 200 h. The most effective process was determined to be repeated fed-batch with a duration of 72 h, producing 57.7–114.5 g/L CA with a yield (YCA) of 0.49–0.64 g/g and a productivity (QCA) of 0.66–1.1 g/L·h. The selectivity of the process, which was initially 90% at the beginning of fermentation, increased to 96.4% after five cycles [131]. The manipulation of the Y. lipolytica SWJ-1b strain, through expression of INU1 and ICL1 genes and deletion of the ACL1 gene, generated transformant № 30, which possesses an enhanced acid-forming capacity (84 g/L CA; YCA = 0.84 g/g and QCA = 0.22 g/L·h) [135]. This strain can assimilate extract from Jerusalem artichoke tubers and produce 68.3 g/L CA with a yield (YCA) of 0.91 g/g. CA has been isolated from culture liquid as crystals with a purity of 96%, with a yield of 67.2% at the isolation stage [45]. A transformant, Y. lipolytica AWG7 INU8, overexpressing the INU1 gene from K. marxianus, can produce 203 g/L of CA from inulin, exhibiting a yield (YCA) of 0.85 g/g and a productivity (QCA) of 0.51 g/L·h during repeated batch mode [49].
Papanikolaou et al. [137] developed a technique to inhibit the TCA cycle by deactivating the PHD1 gene, which encodes 2-methyl-citrate dehydratase. The modification impedes the TCA cycle at the aconitate hydratase level, since 2-methyl-citrate accumulation hinders aconitase, potentially preventing citrate transportation to the mitochondria and ultimately leading to citrate excretion. During nitrogen-limited growth in crude glycerol medium, the modified Y. lipolytica strain (Δphd1) produced 57.7 g/L of CA with a yield of 0.91 g/g, demonstrating a 1.6-fold increase in contrast to the wild-type strain. The recombinant strain also produces considerable amount of CA, even when under excess nitrogen conditions.
Yuzbasheva et al. [136] applied an approach involving the overexpression of genes YlYHM2, which encodes the major mitochondrial citrate transporter, and YlAMPD, encoding adenosine monophosphate deaminase. The obtained recombinant strain can produce 97 g/L CA in glucose-containing medium. This amount is 1.3 times greater than that produced by the wild-type strain. The authors observed that the transformant is unable to assimilate citrate as the only source of carbon.
Therefore, genetic modifications have a significant impact on the production of CA by Y. lipolytica yeast.

8. Adaptive Laboratory Evolution

As an alternative to metabolic engineering, which involves the targeted reorganization of genomes, the method of adaptive laboratory evolution is also utilized for the development of novel strains with desirable characteristics. This approach is not connected to knowledge of metabolic pathways. The process of adaptive laboratory evolution entails prolonged cultivation of microorganisms under specific selective conditions, resulting in hundreds of generations [39][141][142][143]. As noted in the above reviews, the adaptive laboratory evolution usually optimizes parameters such as tolerance to high concentrations of substrates and products, toxic impurities arising from substrates, low pH, and the capacity to assimilate novel carbon sources. Thus, the adaptive laboratory evolution via cell immobilization conducted in shake flasks with an aim to restore the glucose metabolism showed that, after 14 generations of evolution, the mutant strain Y. lipolytica PGC01003 had an increased glucose consumption rate of 0.30 g/L·h in a sugar-rich medium (150 g/L), while the starting strain exhibited poor growth. Furthermore, the productivity of succinic acid in the evolved strain increased by 2.3 times [144]. An adaptive evolution method was utilized to develop a hypertolerant strain, Y. lipolytica, capable of producing succinic acid three times higher than the starting strain in the presence of toxic acetate [145]. The process of adaptive evolution was used effectively to produce a Y. lipolytica strain with greater tolerance to ferulic acid, which is a harmful inhibitor derived from lignocellulose [146]. Comparative transcriptome analysis of the original strain and strain adapted with increasing concentrations of ferulic acid revealed several genes underlying toxicity tolerance enhancements to ferulic acid, and their beneficial contribution was confirmed by metabolic engineering. Daskalaki et al. [147] employed adaptive evolution strategies to enhance lipid accumulation in Y. lipolytica yeast: after 77 generations, a population achieved 44% w/w of lipid, a 30% increase over the starting strain.
Currently, there are no published studies on applying the adaptive laboratory evolution method to produce Y. lipolytica strains with enhanced CA synthesis. Nonetheless, the prolongated experiments conducted in chemostat [121] and variants with recycle [47][108][112][123] may be examined as evolutionary strategies.

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Subjects: Biotechnology & Applied Microbiology
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Svetlana V. Kamzolova
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Update Date: 11 Apr 2024
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