Open Access

Cell factories for insulin production

  • Nabih A Baeshen1,
  • Mohammed N Baeshen1,
  • Abdullah Sheikh1,
  • Roop S Bora1,
  • Mohamed Morsi M Ahmed1, 2Email author,
  • Hassan A I Ramadan1, 3,
  • Kulvinder Singh Saini1 and
  • Elrashdy M Redwan1, 4
Microbial Cell Factories201413:141

DOI: 10.1186/s12934-014-0141-0

Received: 29 June 2014

Accepted: 16 September 2014

Published: 2 October 2014

Abstract

The rapid increase in the number of diabetic patients globally and exploration of alternate insulin delivery methods such as inhalation or oral route that rely on higher doses, is bound to escalate the demand for recombinant insulin in near future. Current manufacturing technologies would be unable to meet the growing demand of affordable insulin due to limitation in production capacity and high production cost. Manufacturing of therapeutic recombinant proteins require an appropriate host organism with efficient machinery for posttranslational modifications and protein refolding. Recombinant human insulin has been produced predominantly using E. coli and Saccharomyces cerevisiae for therapeutic use in human. We would focus in this review, on various approaches that can be exploited to increase the production of a biologically active insulin and its analogues in E. coli and yeast. Transgenic plants are also very attractive expression system, which can be exploited to produce insulin in large quantities for therapeutic use in human. Plant-based expression system hold tremendous potential for high-capacity production of insulin in very cost-effective manner. Very high level of expression of biologically active proinsulin in seeds or leaves with long-term stability, offers a low-cost technology for both injectable as well as oral delivery of proinsulin.

Keywords

Recombinant insulin E. coli Yeast Expression system Posttranslational modifications Transgenic plants

Introduction

The pioneering work of Stanley Cohen and Herbert Boyer, who invented the technique of DNA cloning, signaled the birth of genetic engineering, which allowed genes to transfer among different biological species with ease [1]. Their discovery led to the development of several recombinant proteins with therapeutic applications such as insulin and growth hormone. Genes encoding human insulin and growth hormone were cloned and expressed in E. coli in 1978 and 1979 respectively. The first licensed drug produced using recombinant DNA technology was human insulin, which was developed by Genentech and licensed as well as marketed by Eli Lilly in 1982.

There are more than 300 biopharmaceutical products including therapeutic proteins and antibodies in the market with sales exceeding USD100 billion [2],[3]. Therapeutic monoclonal antibodies have captured the major market share (>USD18 billion) followed by the hormones (>USD11 billion) and growth factors (>USD10 billion) [4]. Biopharmaceuticals approved by the US Food and Drug Administration (FDA) and European Medicines Agency (EMA) from 2004 to 2013 are largely derived from mammalian cell (56%); E. Coli (24%); S. Cerevisiae (13%); Transgenic animals & plants (3%) and insect cells (4%) as shown in Figure 1[5]-[13]. At present, insulin is being produced predominantly in E. coli and Saccharomyces cerevisiae for treatment of diabetic patients.
https://static-content.springer.com/image/art%3A10.1186%2Fs12934-014-0141-0/MediaObjects/12934_2014_Article_141_Fig1_HTML.jpg
Figure 1

Percentage of biopharmaceuticals produced in different expression systems[5]-[13].

Since the early 1920s, diabetic patients were treated with insulin, which was purified from bovine or porcine pancreas. The development in the field of genetic engineering allowed the production of insulin in E. coli and yeast, which have been approved for therapeutic applications in human by FDA [14],[15].

Nowadays, recombinant human insulin is mainly produced either in E. coli or Saccharomyces cerevisiae. Using E. coli expression system, the insulin precursors (IP) are produced as inclusion bodies and fully functional polypeptides are obtained finally by solubilization and refolding procedures [16]. Yeast based expression system yield soluble IP which is secreted into the culture supernatant [17]-[19]. Saccharomyces cerevisiae is the most preferred and predominant yeast for large scale commercial production of insulin, however several other alternate yeast strains have been explored for insulin production [20]-[24]. Besides, E.coli and yeast, mammalian cells, transgenic animals and plant expression systems are also employed as a host for large-scale production of recombinant insulin [25]-[28].

The incidence of diabetes is increasing at an alarming rate and it has been speculated that the number of diabetic patients worldwide would increase to approximately 300 million by the year 2025 [29]. Consequently, the requirement for insulin will increase manifold (approximately more than 16000 kg/ year) and the productivity of current insulin expression system would not be sufficient to meet the future market demands. Efficient expression systems for insulin production are also needed and novel route for insulin administration such as oral or inhalation are to be developed.

Several recombinant protein based drugs, produced by various expression systems are approved by FDA. Among prokaryotes, Escherichia coli has always been preferred for production of recombinant proteins as it offered several advantages including high growth rate, simple media requirement, easy to handle, high yield and very cost effective. However, there are some disadvantages using E. coli expression system, such as loss of plasmid and antibiotic property, unsolicited inducers for gene expression, intracellular accumulation of heterologous proteins as inclusion bodies, improper protein refolding, lack of post- translational modifications (including unable to form disulphide bonds), protein-mediated metabolic burden and stress, endotoxin contamination, poor secretion, proteolytic digestion and complexity in downstream process [30]-[32].

Among yeast strains, Saccharomyces cerevisiae, Hansenulla polymorpha and Pichia pastoris are very commonly used for production of recombinant proteins [21],[24],[33]-[35]. Like E. coli, they grow rapidly and are very easy to handle and amenable to various genetic manipulations. Recombinant proteins produced in yeast are properly folded and glycosylated to a certain extent similar to the one expressed in mammalian cells. Various human therapeutic proteins, including therapeutic monoclonal antibodies are being produced in mammalian cell lines such as Chinese hamster ovary (CHO) and Baby hamster kidney (BHK) cells. Recombinant proteins expressed in mammalian cells are properly folded, glycosylated and generally yield a functionally active protein [36]. However, the production cost of biopharmaceuticals using mammalian expression system is very high due to expensive culture media. However, when we look at the number of approved biopharmaceuticals by United States and/or the European Union for 2013 recorded above average as compared to past five years. The mean rate of approval is 13 as shown in the Figure 2[5]-[13]. Remarkably, the number is same for both the years 2009 and 2013.
https://static-content.springer.com/image/art%3A10.1186%2Fs12934-014-0141-0/MediaObjects/12934_2014_Article_141_Fig2_HTML.jpg
Figure 2

Approval numbers of biopharmaceuticals in United States and/or European Union over the past six years with a trend line showing the mean approval rate[5]-[13].

Structure and function of insulin

The human insulin is comprised of 51 amino acids and has a molecular weight of 5808 Da. It is produced by beta cells of the pancreas and plays a key role in regulating carbohydrate and fat metabolism in the body. Insulin is synthesized as a single polypeptide known as preproinsulin in pancreatic beta cells. Preproinsulin harbours a 24-residue signal peptide, which directs the nascent polypeptide to the endoplasmic reticulum. The signal peptide is cleaved as the polypeptide is translocated into the human of the endoplasmic reticulum resulting in the formation of proinsulin. In the Endoplasmic reticulum, the proinsulin is folded in proper confirmation with the formation of 3 disulphide bonds. Folded proinsulin is then transported to the trans-Golgi network, where it is converted into active insulin by cellular endopeptidases called as prohormone convertases (PC1 and PC2) and exoprotease carboxypeptidase E. The endopeptidases cleaves at two positions, resulting in the release of a fragment termed as C-peptide. The mature insulin, thus formed consists of an A-chain with 21 aminoacids and a B-chain containing 30 aminoacids and both polypeptides linked together by two disulphide bonds. Besides, the A-chain has an intrachain disulphide bond [37],[38].

E. coli expression system for production of insulin

E. coli is a preferred microorganism for large-scale production of recombinant proteins. However, several disadvantages limit its use for production of recombinant biopharmaceuticals. Various post-translational modifications (PTMs) such as glycosylation, phosphorylation, proteolytic processing and formations of disulfide bonds which are very crucial for biological activity, do not occur in E. coli[39],[40]. N-linked glycosylation is the most common posttranslational modification of proteins in eukaryotes. It has been discovered that the bacterium Campylobacter jejuni possess the capability to glycosylate the proteins and it was also shown that a functionally active N-glycosylation pathway could be transferred to E. coli[41]. Although the structure of bacterial N-glycan is different from that observed in eukaryotes, engineering of Campylobacter N-linked glycosylation pathway into E. coli, provides an opportunity to express heterologous proteins in glycosylated form in E. coli. Expression of Pglb oligosaccharyltransferase or (OTase) from C. jejuni in E. coli showed a significant increase in glycopepetide yield [42],[43]. Recently efforts has been made to produce glycosylated proteins with substrates other than native and non-native to E. coli and C.jejuni[44]-[48].

The codon usage of the heterologous protein also plays a major role in determining the expression level of recombinant protein. If the codon usage of heterologous protein differs significantly from the average codon usage of the E. coli host, it could result in very low expression. Usually, the frequency of the codon usage reflects the abundance of their corresponding tRNA. Therefore, significant differences in codon usage could result in premature termination of translation, misincorporation of aminoacids and inhibition of protein synthesis [49]. Expression of heterologous proteins in E. coli can be improved by replacing codons that are rarely found in highly expressed E. coli genes with more favorable major codons. Similarly, co-expression of the genes encoding for a number of the tRNA for rare codon, may enhance the expression of heterologous proteins in E. coli. There are some commercial E. coli strains available that encodes for tRNA for rare codons such as BL21 (DE3) CodonPlus-RIL, BL21 (DE3) CodonPlus-RP (Stratagene, USA) and Rosetta (DE3). BL21 (DE3) CodonPlus-RIL harbors tRNA genes for rare codons like AGG, AGA (arginine), AUA (isoleucine) and CUA (leucine). Similarly, Rosetta (DE3) strain harbors tRNA genes for rare codons like AGG, AGA (arginine), CGG (arginine), AUA (isoleucine), CUA (leucine), CCC (proline) and GGA (glycine). These rare codons have been associated with low expression of proteins in E. coli, hence application of these genetically engineered E. coli host strains may improve the expression level of heterologous proteins and thus might result in higher yield of desired protein [50]-[52]. The use of protease-deficient E. coli strains, which carry mutations that eliminate the production of proteases may also improve the yield of recombinant protein by reducing proteolytic degradation. E. coli strain BL-21, is deficient in two proteases encoded by the lon (cytoplasmic) and ompT (periplasmic) genes. Rather than the external parameters, targeted methods such as modifications in protease or secretion pathways can provide the insight into biology of recombinant proteins [53]. In E. coli, complex and large therapeutic proteins can be secreted in periplasm as it provides an oxidizing environment and help in forming disulphide bonds, which facilitate the proper folding of recombinant proteins and likely to yield reliable N- terminus of expressed protein [54]. Periplasm has advantages over cytoplasm in less protein concentration and proteolytic activity, improve the production titer [55], and enhance the solubility of recombinant protein. Altogether, with these advanced modifications and developments ease the process of target protein production thus accelerating the drug development [56].

Heterologous proteins generally accumulate in E. coli as inclusion bodies, which comprise of insoluble misfolded aggregates of proteins. Use of molecular chaperones may increase the protein solubility and assist in proper folding of recombinant protein. Some of the chaperones prevent aggregation of protein and some assist in refolding and solubilization of misfolded proteins. The most important chaperones in E. coli are GroEL, GroES, DnaK, DnaJ, GrpE and Trigger factor. These chaperones may be used singly, or in combination to enhance the protein solubility in E. coli[57],[58].

Recombinant human insulin was first produced in E. coli by Genentech in 1978, using a approach that required the expression of chemically synthesized cDNA encoding for the insulin A and B chains separately in E. coli[59]. After expressing independently, the two chains are purified and co-incubated under optimum reaction conditions that promoted the generation of intact and bioactive insulin by disulphide bond formation. The first commercial recombinant insulin was developed for therapeutic use in human by this two-chain combination procedure [60]. Another approach involves the expression of a single chemically synthesized cDNA encoding for human proinsulin in E. coli followed by purification and subsequent excision of C-peptide by proteolytic digestion. This approach was more efficient and convenient for large scale production of therapeutic insulin as compared to the two chain combination approach and has been used commercially since 1986 [60]. Eli Lilly followed this technology to produce Humulin, the first recombinant insulin approved in 1982, for the treatment of diabetic patients. These first generation recombinant insulins have an amino acid sequence identical to native human insulin and are preferred over animal derived insulin products [14]. However, advancement in the field of genetic engineering and development of technology to chemically synthesize genes with altered nucleotide sequence, facilitated the development of insulin analogues with altered amino acid sequence. It had been observed that native insulin in commercial preparations usually exist in oligomeric form, as zinc-containing hexamer due to very high concentration, but in blood, biologically active insulin is in monomeric form [61]. Hence, this oligomeric complex should dissociate so that insulin can be absorbed from the site of injection into the blood. Due to this, subcutaneously injected recombinant insulin usually have a slow onset with peak plasma concentration after 2 hours of injection and longer duration of action that last for 6-8 hours [62]. Hence, in order to develop a fast- acting insulin analogue, it was required to modify the amino acids residues whose side chains are involved in dimer or oligomer formation. It has been shown that amino acids residues in insulin B-chain particularly B8, 9,12, 13, 16 and 23-28 play critical role in oligomerization [63],[64]. Lispro, developed by Eli Lilly, was the first fast acting insulin analogue to obtain regulatory approval in 1996, for therapeutic use [60]. Insulin Lispro is engineered in such a way that it has similar amino acid sequence as the native insulin but has an inversion of proline-lysine sequence at position 28 and 29 of the B-chain, which resulted in reduced hydrophobic interactions and thus prevented dimer formations. For commercial production of insulin Lispro, a synthetic cDNA encoding for Lys B28- Pro B29 human proinsulin was expressed in E. coli and insulin Lispro was excised proteolytically from the proinsulin by treating with trypsin and carboxypeptidase. Another rapid-acting insulin analogue, produced in E. coli is Glulisine (Apidra) which was developed by Aventis Pharmaceuticals and approved by US regulatory authorities in 2004. Insulin Glulisine have been generated by replacing B3 asparagine by a lysine and B29 lysine replaced by glutamic acid [14].

To avoid multiple injection, long-acting insulin analogues with prolonged duration of actions have also generated. Insulin Glargine is one of such long-acting insulin analogues, which was developed by Aventis Pharmaceuticals and approved by regulatory authorities of USA and EU in 2000. Insulin Glargine was generated by replacing the C-terminal asparagine of the A-chain with a glycine residue and the C-terminal of the B- chain was modified by adding two arginine residues. These modifications resulted in increase of the isoelectric point (pI) from 5.4 to neutral values. Glargine was produced as proinsulin and expressed in E. coli and was finally formulated at pH 4 in soluble form. However, after subcutaneous administration, it precipitated due to neutral pH in the subcutaneous tissue. Resolubilization of insulin occur slowly, resulting in longer duration for its release in the blood [14].

Yeast expression system for the production of insulin

Yeast is a preferred host for expression of various heterologous proteins that require post-translational modifications for its biological activity. Yeast cell has the ability to carry out numerous post-translational modifications such as phosphorylation, O-linked glycosylation, N-linked glycosylation, acetylation and acylation. Recombinant proteins are expressed in soluble form in yeast and properly folded in functionally active form. Production of biopharmaceuticals using yeast expression system is also very cost effective and is amenable to scale up using large bioreactors. However, one major concern for producing therapeutic glycoprotein for human application is that yeast N-glycosylation is of the high-mannose type, which confers a short half-life in vivo and hyper-immunogenicity and thus render the therapeutic glycoprotein less effective. Various attempts have been made to humanize yeast N-glycosylation pathways in order to produce therapeutic glycoproteins with humanized N-glycosylation structure [65].

The therapeutic proteins produced in yeast are specifically from Saccharomyces cerevisiae and include hormones (insulin, insulin analogues, non-glycosylated human growth hormone somatotropin, glucagon), vaccines (hepatitis B virus surface antigen), uprate oxidase from Aspergillus flavus, granulocyte-macrophage colony stimulating factor, albumin, hirudin of Hirudo medicinalis and human platelets derived growth factor [34]. Like E. coli, yeast derived recombinant biopharmaceuticals majorly intended as therapeutics for infectious diseases or endocrine, metabolic disorders. Alternate yeast strains, besides S. cerevisiae, are being explored for large-scale production of biopharmaceuticals. Specifically, Pichia pastoris has the ability to attain high cell densities by its robust methanol-inducible alcohol oxidase 1 (AOX1) promoter and simple developmental approaches contribute to high quality and quantity of recombinant proteins production. In comparison to Saccharomyces cerevisiae, Pichia pastoris provides a major advantage in the glycosylation of secreted proteins because it does not hyperglycosylate the heterologous proteins. Both yeast strains have a majority of N-linked glycosylation of the high-mannose type, but the length of the oligosaccharides chain added to proteins in Pichia (around 8-14 mannose residues per side chain) is much shorter than those expressed in Saccharomyces cerevisiae (approximately 50-150 mannose residues per side chain), suggesting that glycoproteins produced in Pichia pastoris may be more suitable for therapeutic use in humans [66],[67]. Moreover, very high level of expression of heterologous proteins can be attained in Pichia pastoris, that might constitute about 30% of total cellular protein which is very high as compared to S. cerevisiae[68],[69]. Therefore, Pichia pastoris can be an attractive alternate for large-scale production of recombinant insulin and insulin analogues. Comparing the different insulin production systems where the bacterial expression systems show higher average specific productivity and maximum biomass concentrations are higher in yeast, the overall production space-time yield remains similar as shown in Table 1[70].
Table 1

Comparison of human insulin production systems[70]

Source

E. coli

E. coli

S. cerevisiae

P. pastoris

Destination of product

Cytoplasm

Secreted

Secreted

Secreted

Biomass cell dry weight (g/l)

80, in bioreactor with fed-batch culture

1.2, in shake flask with batch culture

5, in shake flask with batch culture

59, in bioreactor with fed-batch culture

Typical spec. growth rate (1/h)

0.08- 0.12

not specified

< 0.33

<0.03

Typical spec. production rate (mg/gh)

14.2

3.4

0.21

0.375

Product concentration (g/L)

4.34

0.009

0.075

3.075

Productivity (mg/l h)

1,085

4.01

1.04

17

Reference

[71]

[72]

[19]

[73]

Saccharomyces cerevisiae has been extensively used to produce recombinant human insulin since early 1980s [17],[18] and a large proportion of recombinant commercial insulins are produced by this yeast expression system [19],[74]. For efficient expression and secretion of recombinant proinsulin in yeast, insulin construct was engineered to contain the native A-chain and a B-chain lacking the C-terminal B30 threonine, either directly fused or linked via a short synthetic C peptide (like AAK). The cDNA sequence encoding for this construct was fused with α-factor signal sequence of Saccharomyces cerevisiae for secreted expression of proinsulin which gave yield upto 80 mg/ml of insulin. The single chain proinsulin was purified and converted to active insulin by a trypsin-mediated transpeptidation reaction in presence of threonine ester [19]. Besides native recombinant insulin, various insulin analogues are also being produced in S. cerevisiae. Insulin Aspart is another fast-acting insulin analogue, which was produced in S. cerevisiae, developed by Novo Nordisk and approved by US FDA in 2001 for therapeutic use in human. Insulin Aspart was generated by replacing proline residue at position 28 with aspartic acid in the B-chain. This genetic modification resulted in an increase in inter-chain charge repulsion, decrease in self-association and thus causing rapid entry into the blood from the site of subcutaneous injection [63],[75].

Insulin Detemir is another recombinant long-acting insulin analogue that was commercially produced in S. cerevisiae, developed by Novo Nordisk and approved for therapeutic use in human in 2004 by European regulatory authorities. Recombinant Detemir have been generated by removing the threonine residue at the 30 position of the B-chain, and a C14 fatty acid chain covalently attached to the lysine residue at the 29 position of the B-chain. These genetic alterations resulted in the binding of insulin to albumin in plasma, which ensured the slow and constant release of insulin and thus prolonging its duration of action up to 24 hours [76]-[78].

Sacharomyces cerevisiae has been reported for the production of more than 40 different recombinant proteins [79]. A few of which related to diabetes are illustrated in Table 2, along with different characteristics. Few proteins secreted extracellularly by Sacharomyces cerevisiae with α-factor leader sequence being repeatedly used for adequate production of recombinant proteins. Furthermore, a synthetic leader sequence had been developed by Kjeldsen and associates at Novo Nordisk for more efficient protein secretion in yeast [79],[80].
Table 2

Some of the biopharmaceuticals produced by S. cerevisiae[2]

Type

Protein

Therapeutic application

Leader sequence

Titer

Hormones

Insulin Precursor

Diabetes

Synthetic

80 mg/L

 

Glucagon

Diabetes

α-factor

17.5 mg/L

Transgenic plants as host for insulin production

Transgenic plants have been utilized to produce recombinant proteins because of their advantage of cost effectiveness, high quality protein processing, absence of human pathogens, ease of production and presence of eukaryotic machinery for posttranslational modifications. Initially, the human growth hormone was the recombinant protein product extracted from transgenic tobacco plant [81]. After that, numerous different products have developed from plants such as Hepatitis-B-Virus surface antigen, antibodies, industrial proteins and milk proteins.

Recombinant human insulin has been successfully expressed and produced in oilseeds of plant Arabidopsis thaliana[27]. This technology involved the targeted expression of insulin in subcellular organelles known as oilbodies that allowed very high level of expression with easy recovery of recombinant insulin. Oilbodies are storage organelles inside the oilseeds, which comprises of hydrophobic triacylglycerol core encapsulated by phospholipid membrane and an outer wall of proteins known as oleosins. Genetically engineered oil seeds have been generated with recombinant protein specifically targeted to oilbodies as oleosin fusion [27],[82],[83]. Then the oilbodies are easily separated from other seed components by liquid-liquid phase separation, which reduced the number of chromatography steps required to obtain purified insulin. It has been observed that insulin accumulated to high level in transgenic seed (0.13% of total seed protein). Recombinant insulin was cleaved from the oleosin fusion partner and matured with trypsin digestion following oil body purification to yield a biologically active insulin. This study clearly demonstrated that expression of insulin as oleosin fusion protein in plant allow accumulation of large amount of recombinant insulin within the seed and also provide simple downstream purification by centrifugation i.e. oilbody purification. Subsequent maturation to obtain biologically active insulin can be accomplished using standard enzymatic methods currently used for commercial production of insulin from E. coli and yeast. Oilseeds also act as a natural cellular warehouse, where recombinant insulin can be stockpiled until required [27].

In another approach, transgenic plants have been generated, in which, tobacco and lettuce chloroplasts were transformed with human proinsulin comprised of A, B and C-chains fused with the cholera toxin B subunit [28]. It has been observed that, old tobacco leaves accumulated proinsulin upto 47% of total leaf protein and similarly, old lettuce leaves amassed proinsulin up to 53% of total leaf protein. Proinsulin stored in leaves of lettuce was found to be very stable as up to 40% of proinsulin was detected even in senescent and dried leaves as shown in Table 3. Proinsulin from tobacco leaves was extracted with 98% purity and cleaved by Furin protease to release insulin peptides. Oral delivery of unprocessed proinsulin encapsulated in plant cell or by injection into mice revealed lowering of blood glucose levels similar to commercially available insulins. Based on the yield (3 mg of proinsulin/gm of leaves), it was estimated that one acre of tobacco plantation could yield upto 20 million daily doses of insulin per year [28]. C-peptide of proinsulin, which is not present in current commercially available insulin and insulin analogues derived from E. coli and S. cereviciae, would be a great advantage in long-term treatment of diabetic complications such as stimulation of nerve and renal functions. Very high level of expression of biologically active proinsulin in tobacco and lettuce leaves and long-term stability in dried leaves offers a reliable low-cost technology for both injectable as well as oral delivery of proinsulin.
Table 3

CTB cholera toxin B subunit proinsulin expression in tobacco and lettuce chloroplasts[28]

Type of transgenic plant

Tobacco

Lettuce

Destination of the product

Chloroplast

Chloroplast

Percentage of Total leaf protein

47%

53%

Protein yield per gram of leaf tissue

2.92/gm

3.28/gm

Reference

[28]

Conclusion

Over the next 20 years, WHO has estimated that insulin sale would grow from $12 billion to $54 billion globally. Dietary and lifestyle changes are causing dramatic increase in diabetes incidence all over the world. Both Type I and Type II diabetic patients use insulin, however late stage Type II diabetes patients require large doses of insulin as they develop insulin resistance. The dramatic increase in the number of diabetic patients globally and exploration of alternate insulin delivery methods such as inhalation or oral route is bound to escalate the demand for recombinant insulin in near future. Current manufacturing technologies will not be able to meet the growing demand of insulin due to limitation in production capacity and high production cost. Recombinant human insulin is produced predominantly using E. coli and Saccharomyces cerevisiae for therapeutic use in human. However, there is an upmost need to increase the production by several fold of a biologically active insulin and its analogues from E. coli and yeast using latest novel and efficient technologies. Another strategy, using a different expression host other than E. coli and Saccharomyces cerevisiae could be employed. Plant-based expression system hold tremendous potential for high-capacity production of insulin in very cost-effective manner. Very high level of expression of biologically active proinsulin in seeds or leaves with long-term stability, offers a low-cost technology for both injectable as well as oral delivery of proinsulin. Moreover, transgenic seeds can also act as warehouse where recombinant insulin can be stockpiled until required.

Declarations

Acknowledgments

This work was supported by the NSTIP strategic technologies program in the Kingdom of Saudi Arabia (Project No. 10-BIO1257-03). The authors also, acknowledge assistance from the Science & Technology Unit, Deanship of Scientific Research and Deanship of Graduate Studies, King Abdulaziz University, Jeddah, KSA.

Authors’ Affiliations

(1)
Department of Biological Sciences, Faculty of Science, King Abdulaziz University
(2)
Nucleic Acids Research Department, Genetic Engineering and Biotechnology Research Institute (GEBRI), City for Scientific Research and Technology Applications
(3)
Cell Biology Department, Genetic Engineering and Biotechnology Division, National Research Centre
(4)
Protein Research Department, Genetic Engineering and Biotechnology Research Institute, City for Scientific Research and Applied Technology

References

  1. Cohen SN, Chang ACY, Boyer HW, Helling RB: Construction of biologically functional bacterial plasmids in vitro. Proc Natl Acad Sci U S A. 1973, 70: 3240-3244. 10.1073/pnas.70.11.3240.View ArticleGoogle Scholar
  2. Nielsen J: Production of biopharmaceutical proteins by yeast. Landes Biosci Bioengineered. 2013, 4 (4): 207-211. 10.4161/bioe.22856.View ArticleGoogle Scholar
  3. Goodman M: Sales of biologics to show robust growth through to 2013. Nat Rev Drug Discov. 2009, 8: 837-10.1038/nrd3040.View ArticleGoogle Scholar
  4. Aggarwal S: What's fueling the biotech engine 2010 to 2011. Nat Biotechnol. 2011, 29: 1083-1089. 10.1038/nbt.2060.View ArticleGoogle Scholar
  5. Walsh G: Biopharmaceuticals: approvals and approval trends in 2004. Biopharm Int. 2005, 18: 58-65.Google Scholar
  6. Walsh G: Biopharmaceuticals: approval trends in 2005. BioPharm Int. 2006, 9: 58-68.Google Scholar
  7. Walsh G: Biopharmaceuticals: approval trends in 2006. BioPharm Int. 2007, 20: 40-48.Google Scholar
  8. Walsh G: Biopharmaceuticals: approval trends in 2007. BioPharm Int. 2008, 21: 52-65.Google Scholar
  9. Walsh G: Biopharmaceuticals: approval trends in 2008. BioPharm Int. 2009, 22 (10): 68-77.Google Scholar
  10. Walsh G: Biopharmacetiucal approval trends in 2009. BioPharm Int. 2010, 23 (10): 30-41.Google Scholar
  11. Walsh G: Biopharmaceutical benchmarks. Nat Biotechnol. 2010, 28: 917-924. 10.1038/nbt0910-917.View ArticleGoogle Scholar
  12. Walsh G: New biopharmaceuticals. BioPharm Int. 2012, 25: 34-36.Google Scholar
  13. Walsh G: Biopharmaceuticals approval trends in 2013. Biopharm Int. 2013, 26 (4): 54-56.Google Scholar
  14. Walsh G: Therapeutic insulins and their large-scale manufacture. Appl Microbiol Biotechnol. 2005, 67: 151-159. 10.1007/s00253-004-1809-x.View ArticleGoogle Scholar
  15. Ferrer-Miralles N, Domingo-Espin J, Corchero JL, Vazquez E, Villaverde A: Microbial factories for recombinant pharmaceuticals. Microb Cell Fact. 2009, 8: 17-10.1186/1475-2859-8-17.View ArticleGoogle Scholar
  16. Nilsson J, Jonasson P, Samuelsson E, Stahl S, Uhlen M: Integrated production of human insulin and its C-peptide. J Biotechnol. 1996, 48: 241-250. 10.1016/0168-1656(96)01514-3.View ArticleGoogle Scholar
  17. Thim L, Hansen MT, Norris K, Hoegh I, Boel E, Forstrom J, Ammerer G, Fiil NP: Secretion and processing of insulin precursors in yeast. Proc Natl Acad Sci U S A. 1986, 83: 6766-6770. 10.1073/pnas.83.18.6766.View ArticleGoogle Scholar
  18. Markussen J, Damgaard U, Diers I, Fiil N, Hansen MT, Larsen P, Norris F, Norris K, Schou O, Snel L, Thim L, Voigt HO: Biosynthesis of human insulin in yeast via single chain precursors. Diabetologia. 1986, 29: 568A-569A.Google Scholar
  19. Kjeldsen T: Yeast secretory expression of insulin precursors. Appl Microbiol Biotechnol. 2000, 54: 277-286. 10.1007/s002530000402.View ArticleGoogle Scholar
  20. Hollenberg CP, Gellissen G: Production of recombinant proteins by methylotrophic yeasts. Curr Opin Biotechnol. 1997, 8: 554-560. 10.1016/S0958-1669(97)80028-6.View ArticleGoogle Scholar
  21. Gellissen G, Hollenberg CP: A comparison of Saccharomyces cerevisiae, Hansenula polymorpha and Kluyveromyces lactis - a review. Gene. 1997, 190: 87-97. 10.1016/S0378-1119(97)00020-6.View ArticleGoogle Scholar
  22. Romanos M: Advances in the use of Pichia pastoris for high-level gene expression. Curr Opin Biotechnol. 1995, 6: 527-533. 10.1016/0958-1669(95)80087-5.View ArticleGoogle Scholar
  23. Weydemann U, Keup P, Piontek M, Strasser AW, Schweden J, Gellissen G, Janowicz ZA: High-level secretion of hirudin by Hansenula polymorpha - authentic processing of three different preprohirudins. Appl Microbiol Biotechnol. 1995, 44: 377-385. 10.1007/BF00169932.View ArticleGoogle Scholar
  24. Porro D, Sauer M, Branduardi P, Mattanovich D: Recombinant protein production in yeasts. Mol Biotechnol. 2005, 31: 245-259. 10.1385/MB:31:3:245.View ArticleGoogle Scholar
  25. Yanagita M, Nakayama K, Takeuchi T: Processing of mutated proinsulin with tetrabasic cleavage sites to bioactive insulin in the non-endocrine cell line, COS-7. FEBS Lett. 1992, 311: 55-59. 10.1016/0014-5793(92)81366-T.View ArticleGoogle Scholar
  26. Arakawa T, Yu J, Chong DKX, Hough J, Engen PC, Langridge WHR: A plant - based cholera toxin B subunit-insulin fusion protein protects against the development of autoimmune diabetes. Nat Biotechnol. 1998, 16: 934-938. 10.1038/nbt1098-934.View ArticleGoogle Scholar
  27. Nykiforuk CL, Boothe JG, Murray EW, Keon RG, Goren HJ, Markley NA, Moloney MM: Transgenic expression and recovery of biologically active recombinant human insulin from Arabidopsis thaliana seeds. Plant Biotech J. 2006, 4: 77-85. 10.1111/j.1467-7652.2005.00159.x.View ArticleGoogle Scholar
  28. Boyhan D, Daniell H: Low-cost production of proinsulin in tobacco and lettuce chloroplasts for injectable or oral delivery of functional insulin and C-peptide. Plant Biotech J. 2011, 9: 585-598. 10.1111/j.1467-7652.2010.00582.x.View ArticleGoogle Scholar
  29. Wild S, Roglic G, Green A, Sicree R, King H: Global prevalence of diabetes: estimates for the year 2000 and projections for 2030. Diabetes Care. 2004, 27: 1047-1053. 10.2337/diacare.27.5.1047.View ArticleGoogle Scholar
  30. Sahdev S, Khattar SK, Saini KS: Production of active eukaryotic proteins through bacterial expression systems: a review of the existing biotechnology strategies. Mol Cell Biochem. 2008, 307: 249-264. 10.1007/s11010-007-9603-6.View ArticleGoogle Scholar
  31. Arya R, Bhattacharya A, Saini KS: Dictyostelium discoideum-a promising expression system for the production of eukaryotic proteins. FASEB J. 2008, 22: 4055-4066. 10.1096/fj.08-110544.View ArticleGoogle Scholar
  32. Ferrer-Miralles N, Villaverde A: Bacterial cell factories for recombinant protein production; expanding the catalogue. Microb Cell Fact. 2013, 12: 113-10.1186/1475-2859-12-113.View ArticleGoogle Scholar
  33. Kjeldsen T, Pettersson AF, Hach M: Secretory expression and characterization of insulin in Pichia pastoris. Biotechnol Appl Biochem. 1999, 29: 79-86.Google Scholar
  34. Gerngross TU: Advances in the production of human therapeutic proteins in yeasts and filamentous fungi. Nat Biotechnol. 2004, 22: 1409-1414. 10.1038/nbt1028.View ArticleGoogle Scholar
  35. Mansur M, Cabello C, Hernandez L, Pais J, Varas L, Valdes J, Terrero Y, Hidalgo A, Plana L, Besada V, Garcia L, Lamazares E, Castellanos L, Martinez E: Multiple gene copy number enhances insulin precursor secretion in the yeast Pichia pastoris. Biotechnol Lett. 2005, 27: 339-345. 10.1007/s10529-005-1007-7.View ArticleGoogle Scholar
  36. Wurm FM: Production of recombinant protein therapeutics in cultivated mammalian cells. Nat Biotechnol. 2004, 22: 1358-1393. 10.1038/nbt1026.View ArticleGoogle Scholar
  37. Vajo Z, Fawcett J, Duckworth WC: Recombinant DNA technology in the treatment of diabetes: insulin analogs. Endocr Rev. 2001, 22: 706-717. 10.1210/edrv.22.5.0442.View ArticleGoogle Scholar
  38. Ahmad B: Pharmacology of insulin. Br J Diabetes Vasc Dis. 2004, 4: 10-14. 10.1177/14746514040040010201.View ArticleGoogle Scholar
  39. Jenkins N: Modifications of therapeutic proteins: challenges and prospects. Cytotechnology. 2007, 53: 121-125. 10.1007/s10616-007-9075-2.View ArticleGoogle Scholar
  40. Walsh G, Jefferis R: Post-translational modifications in the context of therapeutic proteins. Nat Biotechnol. 2006, 24: 1241-1252. 10.1038/nbt1252.View ArticleGoogle Scholar
  41. Wacker M, Linton D, Hitchen PG, Nita-Lazar M, Haslam SM, North SJ, Panico M, Morris HR, Dell A, Wren BW, Aebi M: N-linked glycosylation in Campylobacter jejuni and its functional transfer into E. coli. Science. 2002, 298: 1790-1793. 10.1126/science.298.5599.1790.View ArticleGoogle Scholar
  42. Feldman MF, Wacker M, Hernandez M, Hitchen PG, Marolda CL, Kowarik M, Morris HR, Dell A, Valvano MA, Aebi M: Engineering N-linked protein glycosylation with diverse O antigen lipopolysaccharide structures in Escherichia coli. Proc Natl Acad Sci U S A. 2005, 102: 3016-3021. 10.1073/pnas.0500044102.View ArticleGoogle Scholar
  43. Wacker M, Feldman MF, Callewaert N, Kowarik M, Clarke BR, Pohl NL, Hernandez M, Vines ED, Valvano MA, Whitfield C, Aebi M: Substrate specificity of bacterial oligosaccharyltransferase suggests a common transfer mechanism for the bacterial and eukaryotic systems. Proc Natl Acad Sci U S A. 2006, 103: 7088-7093. 10.1073/pnas.0509207103.View ArticleGoogle Scholar
  44. Fisher AC, Haitjema CH, Guarino C, Celik E, Endicott CE, Reading CA, Merritt JH, Ptak AC, Zhang S, DeLisa MP: Production of secretory and extracellular N-Linked glycoproteins in Escherichia coli. Appl Environ Microbiol. 2011, 77: 871-881. 10.1128/AEM.01901-10.View ArticleGoogle Scholar
  45. Ihssen J, Kowarik M, Dilettoso S, Tanner C, Wacker M, Thoxy-Meyer L: Production of glycoprotein vaccines in Escherichia coli. Microb Cell Fact. 2010, 9: 61-10.1186/1475-2859-9-61.View ArticleGoogle Scholar
  46. Lizak C, Fan Y, Web TC, Aebi M: N-Linked glycosylation of antibody fragments in Escherichia coli. Bioconjug Chem. 2011, 22: 488-496. 10.1021/bc100511k.View ArticleGoogle Scholar
  47. Pandhal H, Ow SY, Noirel J, Wright PC: Improving N-glycosylation efficiency in Escherichia coli using shotgun proteomics metabolic network analysis, and selective reaction monitoring. Biotechnol Bioeng. 2011, 108: 902-912. 10.1002/bit.23011.View ArticleGoogle Scholar
  48. Chen R: Bacterial expression systems for recombinant protein production: E. coli and beyond. Biotechnol Adv. 2012, 30: 1102-1107. 10.1016/j.biotechadv.2011.09.013.View ArticleGoogle Scholar
  49. Makrides SC: Strategies for achieving high-level expression of genes in Escherichia coli. Microbiol Rev. 1996, 60: 512-538.Google Scholar
  50. Kane JF: Effects of rare codon clusters on high-level expression of heterologous proteins in Escherichia coli. Curr Opin Biotechnol. 1995, 6 (5): 494-500. 10.1016/0958-1669(95)80082-4.View ArticleGoogle Scholar
  51. Trundova M, Celer V: Expression of porcine circovirus 2 ORF2 gene rquires codon optimized E.coli cells. Virus Genes. 2007, 34: 199-204. 10.1007/s11262-006-0043-2.View ArticleGoogle Scholar
  52. Sorensen HP, Sperling-Petersen HU, Mortensen KK: Production of recombinant thermostable proteins expressed in Escherichia coli: completion of protein synthesis is the bottleneck. J Chromatogr B Analyt Technol Biomed Life Sci. 2003, 786: 207-214. 10.1016/S1570-0232(02)00689-X.View ArticleGoogle Scholar
  53. Bill RM, Henderson PJF, Iwata S, Kunji ERS, Michel H, Neutze R, Newstead S, Poolman B, Tate CG, Voge H: Overcoming barriers to membrane protein structure determination. Nat Biotechnol. 2011, 29 (4): 335-340. 10.1038/nbt.1833.View ArticleGoogle Scholar
  54. Huang CJ, Lin H, Yang X: Industrial production of recombinant therapeutics in Escherichia coli and its recent advancements. J Ind Microbiol Biotechnol. 2012, 39: 383-399. 10.1007/s10295-011-1082-9.View ArticleGoogle Scholar
  55. Reilly DE, Yansura DG: Production of monoclonal antibodies in E. coli. Current Trends in Monoclonal Antibodies Development and Manufacturing. Edited by: Shire SJ, Gombotz W, Bechtold-Peters K, Andya J. 2010, 295-308. 10.1007/978-0-387-76643-0_17. Springer, New YorkView ArticleGoogle Scholar
  56. Overton TW: Recombinant protein production in bacterial hosts. Drug Discov Today. 2014, 19 (5): 590-601. 10.1016/j.drudis.2013.11.008.View ArticleGoogle Scholar
  57. Carrio MM, Villaverde A: Role of molecular chaperones in inclusion body formation. Febs Lett. 2003, 537 (1-3): 215-221. 10.1016/S0014-5793(03)00126-1.View ArticleGoogle Scholar
  58. De Marco A: Protocol for preparing proteins with improved solubility by co-expressing with molecular chaperones in Escherichia coli. Nat Protoc. 2007, 2 (10): 2632-2639. 10.1038/nprot.2007.400.View ArticleGoogle Scholar
  59. Chance R, Frank B: Research, development production and safety of biosynthetic human insulin. Diabetes Care. 1993, 16 (3): 133-142.View ArticleGoogle Scholar
  60. Chance R, Glazer N, Wishner K: Insulin Lispro (Humalog). Biopharmaceuticals, an Industrial Perspective. Edited by: Walsh G, Murphy B. 1999, 149-172. 10.1007/978-94-017-0926-2_6. Dordrecht, KluwerView ArticleGoogle Scholar
  61. Blundell T, Dodson G, Hodgkin D, Mercola D: Insulin: the structure in the crystal and its reflection in chemistry and biology. Adv Prot Chem. 1972, 26: 279-402. 10.1016/S0065-3233(08)60143-6.View ArticleGoogle Scholar
  62. Kang S, Creagh F, Peters J, Brange J, Volund A, Owens D: Comparison of subcutaneous soluble human insulin and insulin analogues on meal-related plasma glucose excursions in type-1 diabetic subjects. Diabetes Care. 1991, 14: 571-577. 10.2337/diacare.14.7.571.View ArticleGoogle Scholar
  63. Brange J, Ribel J, Hansen JF, Dodson G, Hansen MT, Havelund S, Melberg SG, Norris K, Norris L, Snel L, Sorensen AR, Voigt HO: Monomeric insulins obtained by protein engineering and their medical implications. Nature. 1988, 333: 679-682. 10.1038/333679a0.View ArticleGoogle Scholar
  64. Brange J, Owens DR, Kang S, Volund A: Monomeric insulins and their experimental and clinical implications. Diabetes Care. 1990, 13 (9): 923-954. 10.2337/diacare.13.9.923.View ArticleGoogle Scholar
  65. Wildt S, Gerngross TU: The humanization of N-glycosylation pathways in yeast. Nat Microbiol. 2005, 3: 119-128. 10.1038/nrmicro1087.View ArticleGoogle Scholar
  66. Grinna LS, Tschopp JF: Size distribution and general structural features of N-linked oligosaccharides from the methylotrophic yeast, Pichia pastoris. Yeast. 1989, 5: 107-115. 10.1002/yea.320050206.View ArticleGoogle Scholar
  67. Tschopp JF, Sverlow G, Kosson R, Craig W, Grinna L: High level secretion of glycosylated invertase in the methylotrophic yeast pichia pastoris. Biotechnology. 1987, 5: 1305-1308. 10.1038/nbt1287-1305.View ArticleGoogle Scholar
  68. Ellis SB, Brust PF, Koutz PJ, Waters AF, Harpold MM, Gingeras TR: Isolation of alcohol oxidase and two other methanol regulatable genes from the yeast Pichia pastoris. Mol Cell Biol. 1985, 5: 1111-1121.View ArticleGoogle Scholar
  69. Tschopp JF, Brust PF, Cregg JM, Stillman C, Gingeras TR: Expression of the lacZ gene from two methanol regulated promoters in Pichia pastoris. Nucleic Acids Res. 1987, 15: 3859-3876. 10.1093/nar/15.9.3859.View ArticleGoogle Scholar
  70. Porro D, Gasser B, Fossati T, Maurer M, Branduardi P, Sauer M, Mattanovich D: Production of recombinant proteins and metabolites in yeasts. Appl Microbiol Biotechnol. 2011, 89: 939-948. 10.1007/s00253-010-3019-z.View ArticleGoogle Scholar
  71. Shin CS, Hong MS, Bae CS, Lee J: Enhanced production of human mini-proinsulin in fed-batch cultures at high cell density of Escherichia coli BL21(DE3)[pET-3aT2M2]. Biotechnol Prog. 1997, 13: 249-257. 10.1021/bp970018m.View ArticleGoogle Scholar
  72. Mergulhao F, Taipa M, Cabral J, Monteiro G: Evaluation of bottlenecks in proinsulin secretion by Escherichia coli. J Biotechnol. 2004, 109: 31-43. 10.1016/j.jbiotec.2003.10.024.View ArticleGoogle Scholar
  73. Gurramkonda C, Polez S, Skoko N, Adnan A, Gabel T, Chugh D, Swaminathan S, Khanna N, Tisminetzky S, Rinas U: Application of simple fed-batch technique to high-level secretory production of insulin precursor using Pichia pastoris with subsequent purification and conversion to human insulin. Microb Cell Fact. 2010, 9: 31-10.1186/1475-2859-9-31.View ArticleGoogle Scholar
  74. Owens DR, Vora JP, Dolben J: Human insulin and beyond: semisynthesis and recombinant DNA technology reviewed. Biotechnology of Insulin Therapy. Edited by: Pickup JC. 1991, 24-41. Blackwell, OxfordGoogle Scholar
  75. Frank B: Manupilation of the position of proline in the B chain produced monomeric insulins. Diabetes. 1991, 40 (Suppl 1): 423A-Google Scholar
  76. Kurtzhals P, Havelund S, Jonassen S, Markussen J: Effect of fatty acids and selected drugs on the albumin binding of a long acting, acylated insulin analogue. J Pharm Sci. 1997, 86 (12): 1365-1368. 10.1021/js9701768.View ArticleGoogle Scholar
  77. Owens DR, Zinman B, Bolli G: Insulins today and beyond. Lancet. 2001, 358: 739-746. 10.1016/S0140-6736(01)05842-1.View ArticleGoogle Scholar
  78. Havelund S, Plum A, Ribel U, Jonassen I, Volund A, Markussen J, Kurtzhals P: The mechanism of protraction of insulin detemir, a long-acting, acylated analog of human insulin. Pharm Res. 2004, 21 (8): 1498-1504. 10.1023/B:PHAM.0000036926.54824.37.View ArticleGoogle Scholar
  79. Hou J, Tyo KEJ, Liu Z, Petranovic D, Nielsen J: Metabolic engineering of recombinant protein secretion by Saccharomyces cerevisiae. FEMS Yeast Res. 2012, 12: 491-510. 10.1111/j.1567-1364.2012.00810.x.View ArticleGoogle Scholar
  80. Kjeldsen T, Hach M, Balschmidt P, Havelund S, Pettersson AF, Markussen J: Prepro-leaders lacking N-linked glycosylation for secretory expression in the yeast Saccharomyces cerevisiae. Protein Expr Purif. 1998, 14: 309-316. 10.1006/prep.1998.0977.View ArticleGoogle Scholar
  81. Staub JM, Garcia B, Graves J, Hajdukiewicz PT, Hunter P, Nehra N, Paradkar V, Schlittler M, Carroll JA, Spatola L, Ward D, Ye G, Russell DA: High-yield production of a human therapeutic protein in tobacco chloroplasts. Nat Biotechnol. 2000, 18: 333-338. 10.1038/73796.View ArticleGoogle Scholar
  82. Van Rooijen GJH, Moloney MM: Plant seed oil-bodies as carriers for foreign proteins. BioTechnology. 1995, 13: 72-77. 10.1038/nbt0195-72.View ArticleGoogle Scholar
  83. Deckers H, Moloney MM, Baum A: The case for recombinant production of pharmaceutical proteins in plants. Annu Rep Med Chem. 1999, 34: 237-245. 10.1016/S0065-7743(08)60586-2.View ArticleGoogle Scholar

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