Isolation, characterization and optimization of culture parameters for production of an alkaline protease isolated from Aspergillus tamarii

Aspergillus tamarii expresses an extracellular alkaline protease that we show to be effective in removing hair from cattle hide. Large quantities of the enzyme will be required for the optimization of the enzymatic dehairing process so the growth conditions for maximum protease expression by A. tamarii were optimized for both solid-state culture on wheat bran and for broth culture. Optimal protease expression occurred, for both cultural media, at initial pH 9; the culture was incubated at 30 °C for 96 h using a 5% inoculum. The crude enzyme was isolated, purified and characterized using MALDI TOF TOF. The alkaline protease was homologous to the alkaline protease expressed by Aspergillus viridinutans. Mention of trade names or commercial products in this publication is solely for the purpose of providing specific information and does not imply recommendation or endorsement by the U.S. Department of Agriculture.     

Characteristics of protease synthesis in Bacteroides splanchnicus NCTC 10825

Studies to determine the physiological and nutritional characteristics of protease synthesis by Bacteroides splanchnicus NCTC 10825 showed that the proteases were constitutive and cell-associated during exponential growth in batch culture. As growth slowed and the bacteria entered the stationary phase, proteases that had accumulated intracellularly were released into the culture media. In continuous cultures, [dilution rate (D)=0.03 h^–1 to D=0.29 h^–1], protease activity was completely cell-bound and maximal during nitrogen-limited growth at high dilution rates. The proteases hydrolysed a relatively restricted range of protein substrates including casein, azocasein and gelatine (comparative maximum rates of hydrolysis were 1.0, 4.1 and 2.7 units mg^–1 protein respectively). B. splanchnicus proteases exhibited arylamidase activities against leucine p-nitroanilide, valylalanine p-nitroanilide and glycylproline p-nitroanilide. Inhibition experiments indicated that the bacterium produced a mixture of serine, thiol and, possibly, metalloproteases. Protease activities were affected by reducing agents and divalent metal ions. Mercaptoethanol at 1 mm was slightly stimulatory; however, dithiortheitol and dithioerythritol (each 10 mm) respectively inhibited protease activities by 91% and 100%. Calcium ions (5 mm) stimulated protease activity by 30%, whereas Mn²⁺ and Mg²⁺ had little or no effect. Protease and arylamidase activities had neutral to alkaline pH optima. Together, these results show that with respect to the types of protease formed and the physiology of the process, B. splanchnicus proteolysis is similar in many respects to that occurring in species belonging to the B. fragilis group. Correspondence to: G. T. Macfarlane     

Alkaline protease from <Emphasis Type="Italic">Bacillus sp.</Emphasis> isolated from coffee bean grown on cheese whey

Two strains of Bacillus, one from a culture collection (B. subtilis ATCC 6633) and a wild type (Bacillus sp. UFLA 817CF) isolated during coffee fermentation in the south of Minas Gerais, Brazil, were evaluated in relation to secretion of alkaline proteases. The strains were grown on nutrient broth, nutrient broth with sodium caseinate and nutrient broth with three different concentrations of cheese whey powder for 72 h. Samples were collected at 24-h intervals to evaluate the proteolytic activity, protein content and cell population. Maximum protease activity was observed after 24-h growth for both the microorganisms, a period that coincided with the end of the exponential phase. The specific activity values were, respectively, 839.8 U/mg for B. subtilis ATCC 6633 and 975.9 U/mg for Bacillus sp. UFLA 817CF. The 60% saturation presented the best results for specific protease activity in all the growth culture media tested with B. sp. UFLA 817CF. Bacillus sp. UFLA 817CF showed highest enzymatic activity at pH 9.0 and 40°C in the three culture media tested. The protease obtained from culture of the wild Bacillus strain presented stability at pH 7.0 and considerable heat stability at 40°C and 50°C, and could be an alternative for the industry to utilize cheese whey to produce proteolytic enzymes.     

A correlative evaluation of morphology and rheology of<Emphasis Type="Italic">Aspergillus terreus</Emphasis> during lovastatin fermentation

Lovastatin, a secondary metabolite, was produced by fermentation process usingAspergillus terreus in an internal loop airlift reactor. It is a highly aerobic fermentation process. Biomass concentration and cell morphology were evaluated and observed to contribute significantly to the high viscosity and pseudoplastic non-Newtonian behavior of the broth. Typical morphological changes over 10 days in the fermentation broth were studied. The viscosity increased from the start of the fermentation with an increasing cell mass content, reached to a maximum of 60 N/m²·s at 160 h and then declined after the branching of the hyphae with the formation of arthrospores. Rheological parameters like consistency index and fluidity index were evaluated. The consistency index was observed to increase from 9.8 to 66.85 N/m², while fluidity index decreased from 0.69 to 0.48 s⁻¹ during 10 days of lovastatin production. A correlation between growth and consistency index of the broth has been evaluated.     

Production of a thermophilic,extracellular alkaline protease by Bacillus stearothermophilus AP-4

A thermophilic Bacillus stearothermophilus strain AP-4 excreting a thermostable alkaline protease, was isolated from a local compost. Maximum activity of protease (250 U/ml) was after 36 h growth in broth at pH 9.0 and at 55°C. The protease was optimally active at pH 9.0 and 55°C and was stable in 5 mm CaCl₂. The enzyme was completely inactivated by PMSF, EDTA and -mercaptoethanol. It is therefore a metal ion-dependent, alkaline, serine protease.R. Dhandapani and R. Vijayaragavan are with the Centre for Plant Molecular Biology & Biotechnology, Tamil Nadu Agricultural University, Coimbatore 641 003, India     

Production,extraction, and thermodynamics protease partitioning from Aspergillus tamarii Kita UCP1279 using PEG/sodium citrate aqueous two-phase systems

Abstract

The protease from Aspergillus tamarii Kita UCP1279 extraction by aqueous two-phase PEG-Citrate (ATPS) systems, using a factorial design 2⁴, was investigated. Then, the variables studied were polyethylene glycol (PEG) molar mass (M_PEG), concentrations of PEG (C_PEG) and citrate (C_CIT), and pH. The responses analyzed were the partition coefficient (K), activity yield (Y) and purification factor (PF). The thermodynamic parameters of the ATPS partition were estimated as a function of temperature. ATPS was able to pre-purify the protease (PF = 1.6) and obtained 84% activity yield. The thermodynamic parameters ΔG°_m (?10.89?kJ mol^?1), ΔH_m (?5.0?kJ?mol^?1) and partition ΔS_m (19.74?J mol^?1 K^?1) showed that the preferential migration of almost all protein contaminants of the crude extract to the salt-rich phase, while the preferred protease was the PEG rich phase. The extracted enzyme presents optimum temperature and pH at range of 40–50?°C and 9.0–11.0, respectively. Moreover, the enzyme was identified as serine protease based on inhibition profile. ATPS showed the satisfactory performance as the first step for Aspergillus tamarii Kita UCP1279 protease pre-purification.     

Real-time fluid dynamics investigation and physiological response for erythromycin fermentation scale-up from 50 L to 132 m<Superscript>3</Superscript> fermenter

The physiological response of erythromycin fermentation scale-up from 50 L to 132 m³ scale was investigated. A relatively high oxygen uptake rate (OUR) in early phase of fermentation was beneficial for erythromycin biosynthesis. Correspondingly, the maximal consistency coefficient (K) reflecting non-Newtonian fluid characteristics in 50 L and 132 m³ fermenter also appeared in same phase. Fluid dynamics in different scale bioreactor was further investigated by real-time computational fluid dynamics modeling. The results of simulation showed that the impeller combination in 50 L fermenter could provide more modest flow field environment compared with that in 132 m³ fermenter. The decrease of oxygen transfer rate (OTR) in 132 m³ fermenter was the main cause for impairing cell physiological metabolism and erythromycin biosynthesis. These results were helpful for understanding the relationship between hydrodynamic environment and physiological response of cells in bioreactor during the scale-up of fermentation process.     

Studies on the production of extracellular protease by Alcaligenes faecalis

Alcaligenes faecalis produced extracellular protease when incubated in media containing protein substrates. Enzyme production was found to be influenced by various culture conditions. Enzyme production was growth-associated, expressed linearity with growth and reached a maximum at the end of the growth phase. Carbohydrates and inorganic nitrogen sources could not be utilized by the bacterium for its growth, and organic nitrogen appeared to be a primary determinant in protease production. Enzyme production reached its maximum level of 171.2 U/ml when the culture was incubated at 30 °C at pH 8.0. Ca²⁺ and Mg²⁺ enhanced the enzyme production. The crude enzyme powder was stable at high alkaline pH and stable upto 6 months at the storage temperature of 0–4 °C. This revised version was published online in July 2006 with corrections to the Cover Date.     

In-situ recovery of butanol during fermentation

End-product inhibition in the acetone-butanol fermentation was reduced by using extractive fermentation to continuously remove acetone and butanol from the fermentation broth. In situ removal of inhibitory products from Clostridium acetobutylicum resulted in increased reactor productivity; volumetric butanol productivity increased from 0.58 kg/(m³h) in batch fermentation to 1.5 kg/(m³h) in fed-batch extractive fermentation using oleyl alcohol as the extraction solvent. The use of fed-batch operation allowed glucose solutions of up to 500 kg/m³ to be fermented, resulting in a 3.5- to 5-fold decrease in waste water volume. Butanol reached a concentration of 30–35 kg/m³ in the oleyl alcohol extractant at the end of fermentation, a concentration that is 2–3 times higher than is possible in regular batch or fed-batch fermentation. Butanol productivities and glucose conversions in fed-batch extractive fermentation compare favorable with continuous fermentation and in situ product removal fermentations.List of Symbols C _g kg/m³ concentration of glucose in the feed - C _w dm³/m³ concentration of water in the feed - F(t) cm³/h flowrate of feed to the fermentor at time t - V(t) dm³ broth volume at time t - V _i dm³ initial broth volume - V _si dm³ volume of the i-th aqueous phase sample - effective fraction of water in the feed Part 1. Bioprocess Engineering 2 (1987) 1–12     

Transport Systems of Ventricaria ventricosa: I/V Analysis of Both Membranes in Series as a Function of [K+] o

The current-voltage (I/V) profiles of Ventricaria (formerly Valonia) membranes were measured at a range of external potassium concentrations, [K⁺] _o , from 0.1 to 100 mm. The conductance-voltage (G/V) characteristics were computed to facilitate better resolution of the profile change with time after exposure to different [K⁺] _o . The resistance-voltage (R/V) characteristics were computed to attempt resolution of plasmalemma and tonoplast. Four basic electrophysiological stages emerged: (1) Uniform low resistance between −60 and +60 mV after the cell impalement. (2) High resistance between +50 and +150 for [K⁺] _o from 0.1 to 1.0 mm and hypotonic media. (3) High resistance between −150 and −20 mV for [K⁺] _o of 10 mm (close to natural seawater) and hypertonic media. (4) High resistance between −150 and +170 mV at [K⁺] _o of 100 mm. The changes between these states were slow, requiring minutes to hours and sometimes exhibiting spontaneous oscillations of the membrane p.d. (potential difference). Our analysis of the I/V data supports a previous hypothesis, that Ventricaria tonoplast is the more resistive membrane containing a pump, which transports K⁺ into the vacuole to regulate turgor. We associate state (1) with the plasmalemma conductance being dominant and the K⁺ pump at the tonoplast short-circuited probably by a K⁺ channel, state (2) with the K⁺ pump ``off' or short-circuited at p.d.s more negative than +50 mV, state (3) with the K<sup>+</sup> pump ``on,' and state (4) with the pump dominant, but affected by high K⁺. A model for the Ventricaria membrane system is proposed. Received: 5 November 1998/Revised: 11 May 1999     

Evaluation of options for harvest of a recombinant E. Coli fermentation producing a domain antibody using ultra scale‐down techniques and pilot‐scale verification

Ultra scale‐down (USD) methods operating at the millilitre scale were used to characterise full‐scale processing of E. coli fermentation broths autolysed to different extents for release of a domain antibody. The focus was on the primary clarification stages involving continuous centrifugation followed by depth filtration. The performance of this sequence was predicted by USD studies to decrease significantly with increased extents of cell lysis. The use of polyethyleneimine reagent was studied to treat the lysed cell broth by precipitation of soluble contaminants such as DNA and flocculation of cell debris material. The USD studies were used to predict the impact of this treatment on the performance and here it was found that the fermentation could be run to maximum productivity using an acceptable clarification process (e.g., a centrifugation stage operating at 0.11 L/m² equivalent gravity settling area per hour followed by a resultant required depth filter area of 0.07 m²/L supernatant). A range of USD predictions was verified at the pilot scale for centrifugation followed by depth filtration. © 2016 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 32:382–392, 2016     

Biomass control in a fixed-bed anaerobic reactor

In order to improve the reliability of fixed-bed anaerobic reactors, the effects of a media and biomass control method were studied using bench scale equipment and mathematical simulation. Test results showed that the allowable volumetric loading rates (kg COD/m³·d) were directly proportional to the packed ratio of the media. Although a reactor completely filled with media (packed media ratio: 100%) could handle an 80% reduction in COD at a loading rate of 11 kg COD/m³·d, a packed reactor half-filled with media (packed media ratio: 50%) could not handle more than 5.5 kg COD/m³·d to achieve the same degree of reduction in COD. Simulation results were based on actual commercial plant operation and showed a practical correlation between COD removal and effective void volume ratio. To achieve a steady reduction of more than 80% in COD, the range of the void volume ratio was presumed to be 0.6 ∼ 0.85.     

Characteristics of the amylase of Arthrobacter psychrolactophilus

Properties of the extracellular amylase produced by the psychrotrophic bacterium, Arthrobacter psychrolactophilus, were determined for crude preparations and purified enzyme. The hydrolysis of soluble starch by concentrated crude preparations was found to be a nonlinear function of time at 30 and 40 °C. Concentrates of supernatant fractions incubated without substrate exhibited poor stability at 30, 40, or 50 °C, with 87% inactivation after 21 h at 30 °C, 45% inactivation after 40 min at 40 °C and 90% inactivation after 10 min at 50 °C. Proteases known to be present in crude preparations had a temperature optimum of 50 °C, but accounted for a small fraction of thermal instability. Inactivation at 30, 40, or 50 °C was not slowed by adding 20 mg/ml bovine serum albumin or protease inhibitor cocktail to the preparations or the assays to protect against proteases. Purified amylase preparations were almost as thermally sensitive in the absence of substrate as crude preparations. The temperature optimum of the amylase in short incubations with Sigma Infinity Amylase Reagent was about 50 °C, and the amylase required Ca⁺² for activity. The optimal pH for activity was 5.0–9.0 on soluble starch (30 °C), and the amylase exhibited a K _m with 4-nitrophenyl-α-D-maltoheptaoside-4,6-O-ethylidene of 120 μM at 22 °C. The amylase in crude concentrates initially hydrolyzed raw starch at 30 °C at about the same rate as an equal number of units of barley α-amylase, but lost most of its activity after only a few hours.     

Xylanase production under solid-state fermentation and its characterization by an isolated strain of <Emphasis Type="Italic">Aspergillus foetidus</Emphasis> in India

Summary A locally isolated strain of Aspergillus foetidus MTCC 4898 was studied for xylanase (EC 3.2.1.8) production using lignocellulosic substrates under solid state fermentation. Corncobs were found as the best substrates for high yield of xylanases with poor cellulase production. The influence of various parameters such as temperature, pH, moistening agents, moisture level, nitrogen sources and pretreatment of substrates were evaluated with respect to xylanase yield, specific activity and cellulase production. Influence of nitrogen sources on protease secretion was also examined. Maximum xylanase production (3065 U/g) was obtained on untreated corncobs moistened with modified Mandels and Strenberg medium, pH 5.0 at 1 5 moisture levels at 30 °C in 4 days of cultivation. Submerged fermentation under the same conditions gave higher yield (3300 U/g) in 5 days of cultivation, but productivity was less. Ammonium sulphate fractionation yielded 3.56-fold purified xylanase with 76% recovery. Optimum pH and temperature for xylanase activity were found to be 5.3 and 50 °C respectively. Kinetic parameters like K_m and V_max were found to be 3.58 mg/ml and 570 μmol/mg/min. Activity of the enzyme was found to be enhanced by cystiene hydrochloride, CoCl₂, xylose and Tween 80, while significantly inhibited by Hg⁺⁺, Cu⁺⁺ and glucose. The enzyme was found to be stable at 40 °C. The half life at 50 °C was 57.53 min. However thermostability was enhanced by glycerol, trehalose and Ca⁺⁺. The crude enzyme was stable during lyophilization and could be stored at less than 0 °C.     

The effect of anti-foam agents on the ultrafiltration of a protease solution

Polydimethylsiloxane and polypropylene glycol-based anti-foam agents adversely influence the ultrafiltration rate of a protease solution with polysulfon membranes. Four propietary agents have been compared, of which Rhodosil 426 R (ex Rhone Poulenc, France), an emulsion of polydimethylsiloxane, proved to have the least influence. With this agent, the relative filtration flux of a protease solution decreased by a factor of two for concentrations of anti-foam agent higher than 0.25 cm³/dm³. A simple, quasisteady-state model developed on the basis of data obtained from total recycle experiments with this anti-foam agent, well predicted the temporal variation of protease concentration during batch ultrafiltration experiments with and without Rhodosil 426 R.List of Symbols A _uf m² total membrane area - C _af dm³/m³ concentration of anti-foam agent - C _af,0 dm³/m³ initial concentration of anti-foam agent in the feed solution - C _e kg/m³ protease powder concentration - C _e,0 kg/m³ initial protease powder concentration in the feed solution - J m³/s ultrafiltration rate - J _w m³/m²s water flow for a clean membrane under processing conditions - R _af rejection coefficient for anti-foam agent - R _e rejection coefficient for protein - RF % relative filtration rate - t s filtration time - V m³ concentrate volume - V ₀ m³ volume to be concentrated - V _t m³ end volume     

Purification and properties of an alkaline protease from alkalophilic Bacillus sp. KSM-K16

Alkaline protease (EC 3.4.21.14) activity, suitable for use in detergents, was detected in the alkaline culture medium of Bacillus sp. KSM-K16, which was originally isolated from soil. The enzyme, designated M protease, was purified to homogeneity from the culture broth by column chromatographies. The N-terminal amino acid sequence was Ala-Gln-Ser-Val-Pro-Trp-Gly-Ile-Ser-Arg-Val-Gln-Ala-Pro-Ala-Ala-His-Asn-Arg-Gly-Leu-Thr-Gly. The molecular mass of the protease was 28 kDa, and its isoelectric point was close to pH 10.6. Maximum activity toward casein was observed at 55°C and at pH 12.3 in 50 mM phosphate/NaOH buffer. The activity was inhibited by phenylmethylsulfonyl flouride and chymostatin. The enzyme was very stable in long-term incubation with liquid detergents at 40°C. The enzyme cleaved the oxidized insulin B chain initially at Leu¹⁵-Tyr¹⁶ and efficiently at ten more sites. Among various oligopeptidyl p-nitro-anilides (pNA) tested, N-succinyl-Ala-Ala-Pro-Phe-pNA was efficiently hydrolyzed by M protease. M protease was precipitated in (NH₄)₂SO₄-saturated acetate buffer (pH 5.0) as plank-like cyrstals.     

An alkaline protease from fresh fruiting bodies of the edible mushroom <Emphasis Type="Italic">Pleurotus citrinopileatus</Emphasis>

A protease was purified from fresh fruiting bodies of the edible mushroom Pleurotus citrinopileatus. The isolation procedure included ion exchange chromatography on DEAE-cellulose, CM-cellulose, and Q-Sepharose and fast protein liquid chromatography-gel filtration on Superdex 75. The protease was unadsorbed on DEAE-cellulose and Q-Sepharose, but adsorbed on CM-cellulose. In sodium dodecyl sulfate-polyacrylamide gel electrophoresis, the protease demonstrated a single band with a molecular mass of 28 kDa. The protease showed an optimal pH at 10 and an optimal temperature at 50°C. The activity of the protease was not affected by EDTA, indicating that it is not a metalloprotease. The protease exhibited a higher activity in the presence of K⁺ and Li⁺, but its activity was potently inhibited by Al³⁺, Cu²⁺, and Hg²⁺ ions. It manifested a K _m of 3.44 mg/ml and a V _max of 0.139 mg ml⁻¹ min⁻¹. It was devoid of ribonuclease and antifungal activities.     

Laboratory production and characterization of a new biosurfactant from <Emphasis Type="Italic">Candida glabrata</Emphasis> UCP1002 cultivated in vegetable fat waste applied to the removal of hydrophobic contaminant

Biosurfactant production by Candida glabrata was studied using vegetable fat waste as substrate. A factorial design was initially carried out to investigate the effects and interactions of waste, yeast extract and glucose on the surface tension after 144 h cultivation. Maximum surface tension reduction was achieved with vegetable fat waste at 5% and yeast extract at 0.2%. The biosurfactant containing cell-free broth retained its surface-active properties after incubation at high temperatures, at a wide range of pH values and salt concentrations. Comparison between three solvent systems for surfactant recovery showed that ethyl acetate extracted both crude extracellular and intracellular biosurfactant with high product recovery. The isolated extracellular biosurfactant showed a CMC of 1% and the surface tension at that point was 24 mN m⁻¹. Preliminary chemical composition revealed the presence of carbohydrates, proteins and lipids. The application of the crude biosurfactant to a soil–water-hydrophobic contaminant system was investigated and the apparent critical micelle concentration was determined at 7% of the broth, although the best oil removal (92.6%) had been obtained with 10% of the cell-free broth. The cost of application of the biosurfactant in soils was estimated based on the cost of a commercial biosurfactant.     

Optimum Culture Conditions for Production of Exfoliative Toxin by Staphylococcus hyicus

Optimum culture conditions for the production of exfoliative toxin by Staphylococcus hyicus (shET) were examined. High shET activity was obtained from the culture filtrate of HI and TY broth inoculated with S. hyicus. The pH in these two media ranged from 7 to 8.5 during bacterial culture, while the lowest pH in TS and BHI broth was less than 6. shET activity in the culture filtrate from TY broth inoculated with 10⁷ CFU of S. hyicus per ml was higher than that in TY broth inoculated with 10⁶ and 10⁸ CFU of bacteria per ml. When shET activity in the culture filtrate was measured under various shaking conditions, the culture filtrate shaken at 75 oscillations per min had the highest shET activity of the five shaking conditions. shET activity of the culture filtrate of TY broth to which protease inhibitor had been added was the same as that of TY broth without inhibitor. shET activity in a shaking culture in an Erlenmeyer flask was also the same as that in sac culture and that in shaking culture using a shaking (Sakaguchi) flask. shET activity in TY broth supplemented with 100 mM glucose was significantly lower than that in TY broth without glucose. Based on the above results, the optimum culture conditions for the production of shET were as follows: inoculation of 3 × 10⁹ CFU of S. hyicus strain P-1 into 300 ml of TY broth in a 2,000-ml Erlenmeyer flask, and incubation at 37 C with shaking at 75 oscillations per min. Then shET activity of the culture filtrate under appropriate culture conditions was measured after various incubation periods. shET activity was detected 6 hr after inoculation, reached the maximum (2⁵³ exfoliative unit/0.1 ml) at 16 hr and decreased between 20 and 48 hr. Thus, the optimum incubation period was determined to be 16 hr. Then the optimum concentration of ammonium sulfate for isolation of shET from the culture filtrate under appropriate culture conditions was examined. The greatest shET activity was obtained from the fraction salted out with 90% saturated ammonium sulfate. Thus, the optimum concentration of ammonium sulfate for the isolation of shET was determined to be 90% saturation.     

Calcium-dependent proteolysis in neural tissue is activated at physiologic intracellular Ca2+ levels and inhibited by some anticonvulsants

The level of calcium-activated neutral protease (CANP) activity in the brain and nerve cord of the crayfish Procambarus clarkii was assayed by measuring the degradation of casein yellow by tissue homogenates. When care was taken to maintain the ionic strength of all incubation media at 0.15M and to buffer the Ca²⁺activity of the media with 5mM EGTA, CANP was found to be very sensitive to Ca²⁺; maximal activity was achieved at 1 × 10^?3M Ca²⁺, with 50% of this maximum present at the physiologic intracellular Ca²⁺activity of 1 × 10^?7M. We found that the anticonvulsant agent phenytoin was without effect on CANP activity while pentobarbital and a relatively new anticonvulsant agent, valproic acid (an eight-carbon branched fatty acid), significantly inhibited CANP activity in a dose-dependent manner. The inhibitory effect of valproic acid was shared by a straight-chain eight-carbon fatty acid, caprylic acid. These findings demonstrate that inhibition of CANP activity is not limited to agents with a specific molecular structure. They also suggest that CANP plays a role in the normal turnover of proteins that control various cellular functions.