Sucrose hydrolysis by invertase using a membrane reactor: effect of membrane cut-off on enzyme performance

Abstracts

Sucrose hydrolysis by invertase [EC.3.2.1.26] produces inverted sugar syrup, an ingredient mainly used in the food industry. To properly catalyze hydrolysis, the enzyme should be reused after this reaction. It is advisable to maintain constant activity over a considerable period. Thus, sucrose hydrolysis was performed in a membrane bioreactor - a continuously stirred tank reactor coupled with an ultrafiltration membrane (UFM) which provides good diffusion and high activity per unit volume. Molecular weight cut-off for soluble invertase UFMs was up to 100kDa. This study focused on the role of UFM invertase cut-off as it is the main element in the process. We demonstrated that both the cut-off and chemical nature of the UFM affected specific invertase activity.

Invertase; Membrane Reactor; Sucrose/hydrolysis

A hidrólise da sacarose através da invertase [EC.3.2.1.26] gera xarope de açúcar invertido, que é usado principalmente como ingrediente na indústria alimentícia. Para ter-se uma hidrólise satisfatória, a enzima deve ser reaproveitada após a reação. É desejável que sua atividade seja mantida constante durante um período considerável de reação. A hidrólise da sacarose foi realizada em um reator com membrana (RM) - que é um reator continuamente agitado acoplado a uma membrana de ultrafiltração (MUF) -, porque apresenta efeitos mínimos de difusão e elevada atividade por unidade de volume. O corte molecular da MUF utilizada para reter a invertase solúvel dentro do MR foi de até 100kDa. Como a invertase é o elemento principal deste processo, este trabalho foi focado no papel do corte molecular da MUF na sua atividade. O corte molecular e a natureza química da membrana-UF mostraram afetar a atividade específica da invertase.

Invertase; Reator de Membrana; Sacarose/hidrólise

INTRODUCTION

Inverted sugar syrup from sucrose hydrolysis is an ingredient used in the food industry. It may also be a source of carbon in fermentation processes. The syrup can be used in food formulation either as a sweetener or a moistener; it also acts as a viscosity, freezing point and water activity reducer of aqueous solutions. As a food component, the syrup colors and aromatizes the product through the Maillard reaction as well as avoiding the crystallization of other formula components.

Sucrose hydrolysis can be catalyzed by hydrochloric acid or by an enzyme such as invertase or α-glucosidase. Despite acidic sucrose hydrolysis being viable for obtaining syrup, the enzymatic process is preferable being a mild reaction (4.5 < pH < 5.0 and 30 ^oC < T < 50 ^oC) (Vitolo, 2004). Moreover, there is no undesirable byproduct formation (Tomotani, Vitolo, 2010). Invertase was chosen for this study because it is inexpensive and abundantly available. In order to properly catalyze the hydrolysis, the enzyme should be reused; it is advisable to keep activity constant over a considerable reaction period. Enzyme recovery is best achieved through immobilization which increases overall process cost due to the need for specific reagents, a carrier, and equipment; enzyme catalytic capacity sometimes diminishes lengthening reaction duration (Nisha et al., 2012). Thus, soluble invertase in a so-called membrane bioreactor (MBR) would be an alternative for hydrolyzing sucrose.

An MBR is a continuous stirred tank reactor (CSTR) with an ultra-filtration membrane (UFM) set in its bottom (Tomotani, Neves, Vitolo, 2005). The MBR presents good diffusion and high activity per unit volume. Invertase, in its soluble form, can be used if the chosen UFM has an adequate molecular weight cut-off (MWCO). As invertase (MW 200kDa) is the main component in the process, this study focused on the role of UFM MWCO on continuous sucrose hydrolysis performed in an MBR.

MATERIAL AND METHODS

Invertase (lyophilized powder containing an activity of 364U/mg_dw where 1U = 1μmol_gluc/min at pH5.0 and 30 °C) was purchased from FLUKA^® (St. Louis, MO, USA) and PBGC polyethersulfone UF membranes (MWCO: 10kDa, 30kDa, 50kDa and 100kDa) were purchased from MILLIPORE^® (Bedford, MA, USA); the 20kDa UF membrane (FS61PP/DDS fluoropolymer) was purchased from DOW DENMARK (Nakskov, Denmark). All of the other chemicals were of analytical grade. Tests were performed in a 10 mL Enzyme MBR (BIOENGINEERING AG, Wald, Germany), previously described by Tomotani, Neves, and Vitolo (2005).

Continuous tests were performed in the MBR in duplicate using 10mL of buffer (0.05M acetic acid/acetate solution at pH5.0) containing soluble invertase (1.53x10^-5 mg_dw/mL). The reactor was coupled to different UF membranes (10kDa, 20kDa, 30kDa, 50kDa, and 100kDa) and fed continuously with a 200mM sucrose solution at a feeding rate of 10 mL/h (1h residence time). The reaction was performed for 30h at 45 °C, agitated at 140 rpm. During tests, reactor internal pressure remained constant at 0.7 bar. Aliquot samples taken every hour from the outlet solution were measured for total reducing sugar (glucose plus fructose) concentration, expressed as µmol of glucose using the conventional Somogyi-Nelson method (Tomotani, Neves, Vitolo, 2005). Invertase activity was expressed as µmol_gluc/min.mg_dw.

RESULTS AND DISCUSSION

Figure 1 shows that a steady state was attained in all tests although its start time differed according to membrane MWCO. Steady state was seen achieved at reaction start with the 10kDa UFM; however it occurred abruptly after 10h continuous feeding with the other UF membranes.

Figure 1
Variation in the logarithm of invertase specific activity (rsp) during continuous hydrolysis of sucrose performed in a membrane reactor coupled to different UF membranes of 10kDa (? ), 20kDa (? ), 30kDa (? ), 50kDa (? ) and 100kDa (?).

A flow process is considered in a steady-state regimen when conditions at all points of the reaction medium remain constant as time changes. Estimates from Figure 1 show at t ≥ 10h that mean values of the logarithm of specific invertase activity were 3.8, 2.6, 2.7, 2.5 and 2.5 for the 10kDa, 20kDa, 30kDa, 50kDa and 100kDa UFM's, respectively.

All UFMs presented different cut-off parameters. The different Log(r_sp) values might have resulted from differences in invertase adsorption intensity on each membrane due to the fact that the enzyme molecules and the membrane surface/matrix have charged chemical groups. The higher the membrane cut-off, the more deeply into the polymeric matrix the enzyme molecules may insert themselves. This could cause structural stress on the overall invertase molecule, which could be directly reflected on its active site, which, in turn, could cause conformational and/or steric constraints. All these effects, in the end, would lead to a less efficient sucrose-invertase interaction. There could also be an electrostatic charge interaction between ionized groups of both invertase and the membrane surface/matrix. The reduction in enzyme-substrate interaction, occurring inside the catalytic site of invertase, may be an intermediary step in sucrose hydrolysis which involves the appearance of a positively charged fructosyl group (Vitolo, 2004). This ion could have its positive charge partially neutralized by the negatively charged groups of the matrix, thus reducing its affinity for water molecules. As a consequence, fructosyl could remain longer inside the catalytic site of invertase, causing a reduction in its turnover number, which, in the end, leads to a reduction in overall specific invertase activity. Prevot-D'Alvise et al. (2004) observed that charges present on both the enzyme (in their case, a commercial protease known as Delvolase^® produced by DSM Food Specialties, Seclin, France) and the membrane (Carbosep, M5-tubular ZrO₂ membrane, produced by Setric Genie Industriel, France) could cause an adsorptive interaction between them, reducing the hydrolysis capability of the protease. Regarding the variation in invertase specific activity against UF membrane cut-off, r_sp decreased as UFM cut-off increased (Table I). Therefore, selecting a UFM with a cut-off lower than enzyme molecular weight (MW) is a required condition but it does not guarantee the highest catalytic activity. In general UFM screening must be performed for any enzyme used in a membrane reactor considering as a limit a UFM cut-off just below enzyme MW. In this work, at first glance, a 100-150kDa UFM was chosen instead of a 10kDa one, in order to deal with an invertase MW of 200kDa.

Table 1
Variation in invertase specific activity (rsp) and the corresponding logarithm of rsp for UF membrane cut-off values

Cut-off	10	20	30	50	100
Log(rsp)	3.8	2.6	2.7	2.5	2.5
rsp(μmolgluc/min.mgdw)	6310	398	501	316	316

Finally, the chemical nature of the UFM seems to have an effect on invertase r_sp. Table I shows the fluoropolymer UFM (cut-off = 20kDa) attaining an r_sp equal to 398 µmol_gluc/min.mg_dw, i.e., a value 20% lower than that attained with a 30kDa polyethersulfone UFM. If cut-off were the only parameter affecting invertase specific activity, this r_sp value would have been between 501 and 6310µmol_gluc/min.mg_dw. Therefore, a coupled effect of both the cut-off value and chemical nature of the UF membrane should be considered for any kind of enzyme used in a membrane reactor.

CONCLUSION

The fluoropolymer membrane (20 kDa) permitted lower specific activity than the polyethersulfone (30kDa) UFM. It was clear that both cut-off and the chemical nature of the UF membrane affected specific invertase activity.

ACKNOWLEDGMENTS

Financial Support was provided by Fapesp (Fundação de Amparo à Pesquisa do Estado de São Paulo), Brazil. The authors would like to thank Philip Barsanti for his invaluable and constructive assessment of the manuscript.

REFERENCES

• NISHA, S.; KARTHICK, A.S.; GOBI, N. A review on methods, application and properties of immobilized enzyme. Che. Sci. Rev. Lett., v.1, p.148-155, 2012.
• PREVOT-D'ALVISE, N.; LESUEUR-LAMBERT, C.; FERTIN-BAZUS, A.; FERTIN, B.; DHULSTER, P.; GUILLOCHON, D. Continuous enzymatic solubilization of alfafa proteins in an ultrafiltration reactor. Enzyme Microb. Technol., v.34, p.380-391, 2004.
• TOMOTANI, E.J.; VITOLO, M. Inverted sugar syrup attained from sucrose hydrolysis using a membrane reactor. Braz. J. Pharm. Sci., v.46, p.571-577, 2010.
• TOMOTANI, E.J.; NEVES, L.C.M.; VITOLO, M. Oxidation of glucose to gluconic acid by glucose oxidase in a membrane bioreactor. Appl. Biochem. Biotechnol., v.121, p.149-162, 2005.
• VITOLO, M. Invertase. SAID, S. PIETRO R.C.L.R. (Eds.). Enzymes as biotechnological agents. Ribeirão Preto: Leggis Summa, 2004. p.207-221.

Publication Dates

• Publication in this collection
  Apr-Jun 2014

History

• Received
  27 Mar 2013
• Accepted
  14 Nov 2013