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Journal of Venomous Animals and Toxins including Tropical Diseases

On-line version ISSN 1678-9199

J. Venom. Anim. Toxins incl. Trop. Dis vol.12 no.3 Botucatu  2006

http://dx.doi.org/10.1590/S1678-91992006000300012 

ORIGINAL PAPER

 

Economic evaluation of snake antivenom production in the public system

 

 

Morais V.; Massaldi H.

Departamento de Desarrollo Biotecnológico y Producción, Instituto de Higiene, Facultad de Medicina, Universidad de la República, Montevideo, Uruguay

Correspondence to

 

 


ABSTRACT

Snake antivenom, an expensive animal product, is presently the only effective treatment for the consequences of snakebite. In Latin America, antivenoms are mainly produced by public institutions with frequent shortages of the necessary supply. Here, we present an economical analysis of the factors affecting production cost, assuming a basic processing batch of 100 L hyperimmune plasma. Three annual production volumes were considered for two typical production technologies. The components of cost were classified as fixed, variable and semi-variable. We found that in all stages of production, fixed cost represents the major contribution to total cost, and is given essentially by manpower cost, particularly for low production volumes. Our estimation shows that antivenom cost can vary from US$ 2.4 to US$ 25 per 10 mL vial, depending on the production volume, the plasma processing technology used and the titer achieved during the immunization stage. We conclude that interested laboratories and authorities of countries with population at risk should consider the possibility of a joint production to improve the process efficiency, lower the product unitary cost and obtain the necessary supply for their own demand or that of other countries in need.

Key words: antivenom, economical cost, immunoglobulins, equine plasma, serum production.


 

 

INTRODUCTION

Snake antivenom is a kind of therapeutic serum which at present constitutes the only effective product to treat the consequences of snakebite, a serious public health problem in many tropical and subtropical countries. Antivenom production is a biotechnological process that involves the use of animal blood as raw material, which is processed and purified before obtaining the final product. Few companies are interested in producing snake antivenoms (20, 21). In Latin America, production is carried out essentially by nonprofit, public institutions (3, 8, 17), whose capacity is generally limited to the country requirements, with little or no surplus (10, 22). This situation has left several non-producing countries deprived of the possibility of acquiring the product (2, 5, 12). In addition, with the incorporation of new quality requirements and new technologies, the cost per dose of snake antivenom has increased considerably in the last years (5, 9).

For the above reasons we considered interesting to gain insight into the components of the production cost in order to achieve better economic control and optimization of public resources and, therefore, to evaluate the possibility of increasing production within reasonable economic limits. In this paper we make an economical analysis of snake antivenom production, focusing on the individual components and their contribution to the overall cost. We applied this analysis to model production cases that can be assimilated to different demands and productive capacities of countries from the Latin American region, but it could be readily extrapolated to other developing countries as well.

 

MATERIALS AND METHODS

Snake Antivenom Production

Figure 1 shows the stages of snake antivenom production. The first stage is the extraction and preparation of snake venom for the immunization of animals, usually horses or sheep (19), from which the active plasma will be obtained. To this end, it is required a serpentarium with enough number of snakes so that antigenic variation due to genetical, regional and/or temporal variations can be minimized (4, 13). For the second stage, there is the need for countryside installations in which animals are maintained and immunized according to a prescribed protocol so that at the end a minimum required antibody titer is obtained in the hyperimmune plasma. In the third stage, the plasma is transported to the processing plant where it is treated to extract and purify the antibody fraction to obtain the final product. Quality control actions according to recommendations of the World Health Organization [WHO] (23) or different pharmacopoeias (6, 1) are included in this stage. Also, for the whole system, availability of mice and guinea pigs is needed to carry out the activities of quality control (11) and snake feeding.

 

 

Theory and Calculation

1. Economic parameters of antivenom production

We restrict our analysis to nonprofit, public institutions, so the cost analysis is the main tool for determination of the product price. The unitary cost of snake antivenom is the cost per ampoule or vial: CA = $/vial; so the annual cost, CT, can be written as:

However, for a given processing volume of plasma, the effective number of vials obtained depends on the overall yield and on the final immunization titer. So, it is convenient to express equation (I) in terms of the number of batches per year, where a batch is defined as the maximum plasma volume treated in one processing cycle. The batch depends only on the equipment processing capacity and not on the plasma characteristics or the purification process efficiency. Thus, from equation (I), by substituting:

No. vials produced/year = No. vials produced/batch * No. batches/year = NVB * NB

It results:

where NVB (effective number of vials produced per batch) is not directly given by the ratio of batch to vial volumes, VB/VV. This parameter includes two corrections in the ratio. One is the ratio of the final immunization titer, Tfi, to the minimum required titer, Tmi, and the other is the overall process yield, in terms of percentage activity recovery from the initial plasma, Ra. Therefore, NVB can be expressed as:

where VB is the batch processing volume and VV is the volume of each vial. Equations (II) and (III) show that NVB is higher, and therefore CA is lower, when Tfi and/or Ra are higher.

2. Components of costs for each production stage

Conventionally, two types of costs are considered in any economic analysis of production: fixed costs (CF) and variable costs (CV). CV varies directly in proportion to the volume of production in a given period of time. CF is independent of fluctuations in the production volume and should remain constant within a wide range of production values. However, it should be taken into account that the fixed costs cannot remain constant if the production volume increases above the production system capacity. This may happen because of having reached either the maximum capacity of the available equipment or the maximum frequency of processing cycles.

In addition to these types, there are costs that have a fixed root and a variable component. These may be called semi-variable costs and we denoted them as CSV. The total production annual cost, CT, is equal to the sum of all of them:

The cost components for each production stage are shown in Table 1 on an annual basis. The calculation indexes and the economic values derived from them, presented in the subsequent Tables, are assumed to be representative, with expected local variations of the prevailing conditions in Latin American countries. We assume that, in all cases, the equipment, processes and installations comply with the requirements of good manufacturing practices.

 

 

The cost of manpower, MP, a typically variable cost, was presented here as a fixed cost to reflect the reality of public institutions, where specialized personnel cannot be hired on a campaign basis and is part of the permanent staff. We also included technical and supporting personnel of production and control in all categories. As a feasible working hypothesis, it is assumed that when not involved in production, this personnel is performing R & D activities. On the other hand, for the reasons explained earlier, the variable costs were expressed in terms of number of batches per year, NB. Also, installation and equipment maintenance, considered as a semi-variable cost, was expressed as partly dependent on NB.

We compared the costs involved in two widely accepted methods of antivenom production: peptic digestion of whole plasma plus ammonium sulphate purification, with F(ab')2 fragment as product (7, 14), and caprylic acid extraction together with purification of whole immunoglobulins (18). In both cases, the final product is in liquid form. These processes differed essentially in the percent recovery of active antibodies, which is in the order of 30% for the F(ab')2 product (15) and about 60% for whole purified immunoglobulins (18). We also applied the analysis for two possible final immunization titers of hyperimmune plasma and three qualitatively different batch-processing volumes. For modeling purposes, we assumed 100 L as the maximum processing volume of plasma per campaign (basic plasma processing batch). For processing volumes above 100 L per year, the production demand is fulfilled by repeating the plasma treating process with the basic batch as many times as needed or possible within the period (e.g. for 1,000 L / year, 10 cycles).

 

RESULTS

Tables 2 and 3 show the cost components for stages 1 and 2 of antivenom production (Figure 1), namely venom preparation and hyperimmune plasma obtainment, respectively. These stages are common and prior to the plasma treating process in stage 3. The economic contribution of stages 1 and 2 to the third stage is clearly constant, regardless of the efficiency of the plasma-treating process or the final immunization titer. Therefore, the respective final costs of those stages are directly included as components of the fixed cost in the analysis of the third stage, presented in Tables 4 and 5. These tables show the cost components for the two types of plasma-treating processes mentioned earlier, and for two possible titer immunization ratios, for processing volumes of 100, 200, and 1,000 L in all cases, corresponding to a number of basic batches, NB = 1, 2, and 10.

 

 

 

 

 

 

 

 

DISCUSSION

According to Table 2 (A. Venom preparation), there is no discrimination between costs in terms of fixed or variable, and the components are independent of the production volume. This happens because the snake population is high enough to support the annual provision of venom for large production volumes; therefore, stage A. behaves as a fixed cost for the whole production process.

Table 3 (B. Hyperimmune plasma) shows that the cost increases only slightly for production volumes between 100 and 200 L, but it becomes much higher at 1,000 L. This reflects the possibility of using the same group of horses to obtain 100 or 200 L plasma per year by performing two annual immunizations in the 200 L case. However, to obtain 1,000 L plasma with two annual immunizations it is necessary to increase the number of horses by about five. Similarly, maintenance cost increases with the production volume but not in direct proportion. This is due to the formula indicated in Table 1, which reflects the existence of a maintenance cost, even without production (NB = 0), plus a term that depends on the annual usage of the equipment and installations. It is also noticeable the strong contribution of maintenance (frequently neglected or underestimated in institutional budgets) to the total cost.

The costs of consumables, services and filling are clearly variable. We assumed that filling is carried out in installations outside the producing institution, which is more convenient for laboratories of relatively low production volumes. The single annual batch of 100 L approaches the situation prevailing in Uruguay, where the health system demand due to snakebite accidents is very limited. For Uruguay, a typical dose is made of 4-8 vials, with each vial neutralizing 25 mg of Bothrops alternatus venom, similar to that used by other countries of the region like Argentina and Brazil (16). In some countries, the dose administered to the patient is only one 10-mL vial (5), which is a consequence of the scarcity and high cost of the antivenom rather than a therapeutic rationale.

Tables 4 and 5 show the cost components for the whole production system and the total and unitary costs for each situation presented. The numbers are self-explanatory. It is evident that the cost per vial decreases as the production volume increases, which is due to the high contribution of the fixed costs to the total cost in all stages. Moreover, the manpower cost for production and R & D taken together, as considered here, represents a great part of the fixed cost, particularly for low production volumes. We have assumed that the production volume can only be increased by the repeated use of the same equipment in different cycles, thereby increasing the number of processed batches per year. A possible alternative analysis to cover a large increase in production would consider the use of large-scale equipment and technology, in which the corresponding fixed costs would increase accordingly, particularly in stage C. Of course, this is unavoidable if the situation requires processing batches of 1,000 L to fulfill an annual demand 10 times higher, as would be the case of some tropical countries with high incidence of snakebite accidents. In this situation, it would be possible to carry out a cost analysis similar to that presented here, which at least qualitatively should provide similar relationships between cost components. In any case, from a technological point of view, a quantitative aspect to be emphasized is the direct increase of the effective number of vials produced and, concomitantly, the reduction of the cost per vial – see equation (II) – which can be determined by using a highly efficient plasma process and/or a good final immunization titer.

We conclude that for snake antivenom production, the large contribution of the fixed costs to the total cost makes it convenient, whenever possible, to increase the number of vials (doses) produced per year within the same facility and technology. Since many producing countries only yield the necessary number of doses to cover the country requirements, their production systems are idle during more or less extensive periods, which causes an augment of the unitary cost. One alternative to overcome this problem is that interested laboratories consider the possibility of establishing a joint production facility to serve the necessities of the group and, eventually, those of other countries in need of antivenom and outside the region.

 

ACKNOWLEDGEMENTS

The financial support of CSIC, Uruguay, is gratefully acknowledged.

H. A. Massaldi is a member of the research career of CONICET, Argentina.

 

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Correspondence to:
Hugo Massaldi
Av. A. Navarro 3051
11600 Montevideo, Uruguay
Phone: (598-2) 487-1288 int 1122. Fax: (598-2) 487-3073
Email: massaldi@higiene.edu.uy or massaldi@anlis.gov.ar

Received: December 5, 2005
Accepted: June 1, 2006
Abstract published online: June 14, 2006
Full paper published online: August 31, 2006

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